CN201165470Y - An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device - Google Patents
An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device Download PDFInfo
- Publication number
- CN201165470Y CN201165470Y CNU2007201733255U CN200720173325U CN201165470Y CN 201165470 Y CN201165470 Y CN 201165470Y CN U2007201733255 U CNU2007201733255 U CN U2007201733255U CN 200720173325 U CN200720173325 U CN 200720173325U CN 201165470 Y CN201165470 Y CN 201165470Y
- Authority
- CN
- China
- Prior art keywords
- hydrogen
- plasma
- rich gas
- reforming
- plasma generator
- 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.)
- Expired - Fee Related
Links
Images
Classifications
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
Landscapes
- Hydrogen, Water And Hydrids (AREA)
Abstract
本实用新型涉及新能源领域,提供一种高效、快速、结构紧凑的车载富氢气体制备装置,用于在短时间内制备车载富氢气体,该装置为圆筒状结构,包括等离子体发生器(1)和等离子体反应器(2)两部分,两者相连接,等离子体发生器(1)具有进气口(4),进气口(4)设置为偏心式,等离子体发生器(1)的内腔被分为两个气室,下气室为燃料的预混室,整个装置为立式,采用不锈钢材料制作,该装置基于等离子体化学反应特性,利用等离子体重整法对碳氢燃料进行重整制氢,具备启动快、效率高、成本低、易于实现等优点,大大提高了制氢速度与制氢效率。
The utility model relates to the field of new energy, and provides an efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device for preparing vehicle-mounted hydrogen-rich gas in a short time. The device has a cylindrical structure and includes a plasma generator (1) and plasma reactor (2) two parts, both are connected, and plasma generator (1) has air inlet (4), and air inlet (4) is arranged as eccentric type, and plasma generator ( 1) The inner cavity is divided into two gas chambers, the lower gas chamber is a fuel premixing chamber, the whole device is vertical, made of stainless steel, the device is based on the chemical reaction characteristics of plasma, and uses plasma reforming method to treat carbon The reforming of hydrogen fuel to produce hydrogen has the advantages of fast start-up, high efficiency, low cost, and easy implementation, which greatly improves the speed and efficiency of hydrogen production.
Description
技术领域 technical field
本实用新型属于新能源领域,该装置的作用是使碳氢燃料在常温常压下快速地与空气发生部分氧化反应,产生富氢气体,从而提高汽车的燃烧效率、降低有害排放。The utility model belongs to the field of new energy, and the function of the device is to make hydrocarbon fuel undergo partial oxidation reaction with air rapidly under normal temperature and pressure to generate hydrogen-rich gas, thereby improving the combustion efficiency of automobiles and reducing harmful emissions.
背景技术 Background technique
目前,世界性的能源危机、环境污染等问题日益严重。而汽车作为石油的主要消耗者,它消耗的石油资源越来越多,其行驶时排出的气体(态)污染物(CO、NOx、HC)、微粒污染物、蒸发排放物等也已成为城市空气污染的主要来源。因此,开发廉价、清洁的新能源已成为汽车工业迫在眉睫的任务。At present, the global energy crisis, environmental pollution and other problems are becoming more and more serious. As the main consumer of petroleum, automobiles consume more and more petroleum resources, and the gas (state) pollutants (CO, NO x , HC), particulate pollutants, and evaporative emissions emitted during driving have also become Major source of urban air pollution. Therefore, the development of cheap and clean new energy has become an urgent task for the automobile industry.
氢气的热值是140kJ/g,大约为汽油的三倍,被认为是取代矿物燃料的理想能源。虽然氢罐的最大压力已达70MPa,但还是不能满足续驶里程的要求,并且还存在安全隐患等问题,而车载富氢气体制备装置则可以较好地解决上述问题,是最现实的移动氢源的选择之一。目前,车载碳氢燃料重整制氢的方法有化学重整法和等离子体重整法两种。The calorific value of hydrogen is 140kJ/g, about three times that of gasoline, and is considered to be an ideal energy source to replace fossil fuels. Although the maximum pressure of the hydrogen tank has reached 70MPa, it still cannot meet the requirements of driving mileage, and there are still problems such as safety hazards. The vehicle-mounted hydrogen-rich gas preparation device can better solve the above problems and is the most realistic mobile hydrogen. One of the source choices. At present, there are two methods of reforming vehicle-mounted hydrocarbon fuels to produce hydrogen: chemical reforming and plasma reforming.
(1)化学重整法(1) chemical reforming method
化学重整法的原理是在催化剂的作用下,使碳氢燃料发生化学变化产生氢气,其中包括水蒸气重整、部分氧化重整和自热重整。水蒸气重整制氢是比较成熟的技术,在催化剂的作用下,可将碳氢燃料中的氢与水中的氢都转化成氢气,因此其产氢率高,但由于该反应为吸热反应,故需外部供热,因此整个系统的热效率低。部分氧化重整制氢在工业制氢领域是比较成熟的技术,它甚至可将重油转化为富氢氢气,其产氢率比水蒸气重整的低,并且空气中的氮气会稀释产气中氢气的体积百分含量,但由于该反应为放热反应,故外部供热少,整个系统的热效率较高,并且启动时间短、动态响应快。自热重整即将吸热的水蒸气重整和放热的部分氧化重整结合到一起,并在一定条件下实现热量的自平衡,该重整方式的产氢效率高、能量利用率高,但是容易出现局部过热现象(即“热点”)。The principle of chemical reforming is to chemically change hydrocarbon fuels to produce hydrogen under the action of a catalyst, including steam reforming, partial oxidation reforming and autothermal reforming. Hydrogen production by steam reforming is a relatively mature technology. Under the action of a catalyst, hydrogen in hydrocarbon fuels and hydrogen in water can be converted into hydrogen, so its hydrogen production rate is high. However, because the reaction is an endothermic reaction , so external heating is required, so the thermal efficiency of the entire system is low. Hydrogen production by partial oxidation reforming is a relatively mature technology in the field of industrial hydrogen production. It can even convert heavy oil into hydrogen-rich hydrogen. Its hydrogen production rate is lower than that of steam reforming, and the nitrogen in the air will dilute the produced gas. The volume percentage of hydrogen, but because the reaction is an exothermic reaction, there is less external heat supply, the thermal efficiency of the whole system is higher, and the start-up time is short and the dynamic response is fast. Autothermal reforming combines endothermic steam reforming and exothermic partial oxidation reforming, and realizes self-balancing of heat under certain conditions. This reforming method has high hydrogen production efficiency and high energy utilization rate. However, it is prone to localized overheating (ie "hot spots").
(2)等离子体重整法(2) Plasma reforming method
等离子体重整(Plasma reforming)是近10年才出现的一种重整制氢的方法,它是利用气体通过高压电极间的空间时,电极间流动的电子将使气体分子分裂,产生物质的第四态--等离子体。由于等离子体中存在活性自由基(如O、OH、O3等),因而可引发部分化学反应的发生。由于等离子体的能量密度高,不需要催化反应器,因此可大幅度降低重整器的大小和质量。等离子体重整装置结构简单、制氢速度快、启动快、可以不用催化剂、可在常温常压下、极短的时间、较小的反应空间内引发制氢反应,因此被认为是多变条件下小规模生产氢气的理想选择。众所周知,PEMFC的阴极Pt催化剂会CO中毒,目前能够耐受的CO最大允许值约为10ppm,利用Plasma重整法可使碳氢燃料在高温下迅速发生分解反应,该反应的产物为炭和氢气,不产生使Pt催化剂中毒的气体CO,以及温室气体CO2。虽然等离子体发生器需要消耗电能来产生等离子体,但其消耗的电能仅为几十瓦,相当于一个车前照灯消耗的能量,相对其消耗的能量,其节省的能量更多,并且可以使燃烧产物更为清洁。等离子体重整的另一大优势是其可重整的燃料很多,像酒精、柴油、生物垃圾、天然气等。Plasma reforming (Plasma reforming) is a method of reforming hydrogen production that has only appeared in the past 10 years. It uses the gas to pass through the space between high-voltage electrodes, and the electrons flowing between the electrodes will split the gas molecules to produce the first material. Four states - plasma. Due to the presence of active free radicals (such as O, OH, O 3 , etc.) in the plasma, some chemical reactions can be initiated. Since the high energy density of the plasma does not require a catalytic reactor, the size and mass of the reformer can be greatly reduced. The plasma reforming device has a simple structure, fast hydrogen production speed, fast start-up, no catalyst, can initiate hydrogen production reaction at room temperature and pressure, in a very short time, and in a small reaction space, so it is considered to be a Ideal for small-scale production of hydrogen. It is well known that the cathode Pt catalyst of PEMFC will be poisoned by CO, and the maximum allowable value of CO that can be tolerated is about 10ppm. The Plasma reforming method can make the hydrocarbon fuel decompose quickly at high temperature, and the products of this reaction are carbon and hydrogen. , does not produce the gas CO that poisons the Pt catalyst, and the greenhouse gas CO 2 . Although the plasma generator needs to consume electric energy to generate plasma, the electric energy it consumes is only tens of watts, which is equivalent to the energy consumed by a car headlight. Compared with the energy consumed by it, it saves more energy and can Make combustion products cleaner. Another advantage of plasma reforming is that it can reform many fuels, such as alcohol, diesel, biological waste, natural gas, etc.
由此可见,化学重整法与等离子体重整法制氢原理的不同之处是它们激发化学反应的活性物质不同。化学重整法的活性物质是催化剂,而等离子体重整法的活性物质是活性自由基。但是催化剂往往需要在高温下才能发挥其活性,因此需要加热,使得消耗的能量更多,并且加热时间一般需要几分钟,因此利用化学重整法的制氢装置启动较慢。但是等离子体重整法不需要催化剂,在常温下就可发生反应,因此利用等离子体重整法的制氢装置启动快。It can be seen that the difference between the hydrogen production principle of the chemical reforming method and the plasma reforming method is that they have different active substances to stimulate chemical reactions. The active substance of the chemical reforming method is a catalyst, while the active substance of the plasma reforming method is an active free radical. However, the catalyst often needs to be heated at high temperature to exert its activity, so it needs to be heated, which consumes more energy, and the heating time generally takes several minutes, so the hydrogen production device using the chemical reforming method is slow to start. However, the plasma reforming method does not require a catalyst, and the reaction can occur at room temperature, so the hydrogen production device using the plasma reforming method starts quickly.
实用新型内容:Utility model content:
为解决上述问题,本实用新型提供一种低成本、启动快、高效、结构紧凑的车载富氢气体制备装置。In order to solve the above problems, the utility model provides a vehicle-mounted hydrogen-rich gas preparation device with low cost, fast start-up, high efficiency and compact structure.
采用的技术方案如下:车载富氢气体制备装置,其为圆筒状结构,包括相互连接的等离子体发生器和等离子体反应器两部分,等离子体发生器包括进气口,进气口设置为偏心式,等离子体发生器的内腔被分为两个气室,下气室为燃料的预混室,整个装置为立式,采用不锈钢材料制作。The technical scheme adopted is as follows: a vehicle-mounted hydrogen-rich gas preparation device, which is a cylindrical structure, including two parts, a plasma generator and a plasma reactor connected to each other, the plasma generator includes an air inlet, and the air inlet is set as Eccentric type, the inner cavity of the plasma generator is divided into two air chambers, the lower air chamber is the fuel premix chamber, the whole device is vertical and made of stainless steel.
偏心式进气口设计,使得进气产生涡流,增长了气体与电弧的接触时间,以便产生更多的等离子体,等离体发生器内腔的下气室作为燃料的预混室,使燃料能更好地混合,整个装置为立式,气体从下往上流,由于氢气的密度小,该结构有利于氢气的溢出。The eccentric air inlet design makes the air intake vortex, prolongs the contact time between the gas and the arc, so as to generate more plasma, and the lower chamber of the plasma generator inner cavity is used as a fuel premix chamber, so that the fuel It can be mixed better. The whole device is vertical, and the gas flows from bottom to top. Due to the low density of hydrogen, this structure is conducive to the overflow of hydrogen.
车载富氢气体制备装置还以去除侧电极的火花塞作为负极,并将火花塞安装在等离子体发生器沿轴向的一端,制氢装置接地作为正极,以火花放电产生等离子体。在常温常压下,当碳氢燃料和空气的混合物进入等离子体发生器后,经火花放电产生等离子体。之后,反应物进入等离子体反应器,在该区域,等离子体将促进燃料与空气发生部分氧化反应,在短时间内产生富氢气体。The vehicle-mounted hydrogen-rich gas preparation device also uses the spark plug removed from the side electrode as the negative electrode, and the spark plug is installed at one end of the plasma generator along the axial direction, and the hydrogen production device is grounded as the positive electrode, and the plasma is generated by spark discharge. Under normal temperature and pressure, when the mixture of hydrocarbon fuel and air enters the plasma generator, plasma is generated by spark discharge. Afterwards, the reactants enter the plasma reactor, where the plasma promotes the partial oxidation of fuel and air, producing hydrogen-rich gas in a short period of time.
该车载富氢气体制备装置的特点是:利用等离子体重整法重整制氢,制氢速度与制氢效率高、成本低、启动快、结构紧凑,并且易于实现。The characteristics of the vehicle-mounted hydrogen-rich gas preparation device are: using plasma reforming method to reform and produce hydrogen, with high hydrogen production speed and hydrogen production efficiency, low cost, fast start-up, compact structure, and easy implementation.
附图说明 Description of drawings
图1是车载富氢气体制备装置的结构图;Fig. 1 is a structural diagram of a vehicle-mounted hydrogen-rich gas preparation device;
图2是车载富氢气体制备装置的A-A向视图;Fig. 2 is the A-A direction view of the vehicle-mounted hydrogen-rich gas preparation device;
图3是车载富氢气体制备装置的应用举例示意图。Fig. 3 is a schematic diagram of an application example of a vehicle-mounted hydrogen-rich gas preparation device.
图中标号说明Explanation of symbols in the figure
1-等离子体发生器;2-等离子体反应器;3-电极安装孔;4-进气口;5-出气口;6-点火控制单元;7-已去除侧电极的火花塞;8-净化器;9-氢燃料汽车发动机;10-接地。1-plasma generator; 2-plasma reactor; 3-electrode installation hole; 4-air inlet; 5-gas outlet; 6-ignition control unit; 7-spark plug with side electrode removed; 8-purifier ; 9-hydrogen fuel vehicle engine; 10-grounding.
具体实施方式 Detailed ways
该车载制氢装置的结构图如图1所示。碳氢燃料和空气的混合物从进气口4进入等离子体发生器1,经火花塞放电产生等离子体。之后,反应物进入等离子体反应器2,在该区域,等离子体促进燃料与空气发生部分氧化反应,在短时间内产生富氢气体。制得的富氢气体从出气口5流出。The structural diagram of the vehicle-mounted hydrogen production device is shown in Figure 1. The mixture of hydrocarbon fuel and air enters the
在实际应用中,可单独使用一个该车载制氢装置,也可将两个或多个该车载制氢装置并联使用。可设计为如图2所示的氢燃料汽车车载制氢系统。该系统使用1个车载制氢装置,用点火控制器6控制火花放电。燃料与空气的混合气从进气口4进入车载制氢装置,在火花放电等离子体的作用下重整得到富氢气体,然后经过净化器8,最后进入氢燃料汽车发动机9。In practical applications, one vehicle-mounted hydrogen production device can be used alone, or two or more vehicle-mounted hydrogen production devices can be used in parallel. It can be designed as an on-board hydrogen production system for hydrogen fuel vehicles as shown in Figure 2. The system uses a vehicle-mounted hydrogen production device and uses an
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201733255U CN201165470Y (en) | 2007-09-24 | 2007-09-24 | An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007201733255U CN201165470Y (en) | 2007-09-24 | 2007-09-24 | An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201165470Y true CN201165470Y (en) | 2008-12-17 |
Family
ID=40190852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007201733255U Expired - Fee Related CN201165470Y (en) | 2007-09-24 | 2007-09-24 | An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201165470Y (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102802334A (en) * | 2012-07-31 | 2012-11-28 | 北京航空航天大学 | Sliding-arc-discharge plasma generation device loaded with magnetic field |
| CN104477848A (en) * | 2014-12-02 | 2015-04-01 | 中山大学 | Hydrogen production method by using plasma reforming engine fuel |
| CN109896501A (en) * | 2017-12-11 | 2019-06-18 | 中国科学院大连化学物理研究所 | A kind of reforming hydrogen production device and the method using the device hydrogen manufacturing |
-
2007
- 2007-09-24 CN CNU2007201733255U patent/CN201165470Y/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102802334A (en) * | 2012-07-31 | 2012-11-28 | 北京航空航天大学 | Sliding-arc-discharge plasma generation device loaded with magnetic field |
| CN104477848A (en) * | 2014-12-02 | 2015-04-01 | 中山大学 | Hydrogen production method by using plasma reforming engine fuel |
| CN109896501A (en) * | 2017-12-11 | 2019-06-18 | 中国科学院大连化学物理研究所 | A kind of reforming hydrogen production device and the method using the device hydrogen manufacturing |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6977082B2 (en) | Ammonia decomposition equipment and system and hydrogen production method | |
| CN104953147B (en) | A self-supply hydrogen fuel cell system and its working method | |
| CN115636391A (en) | Hydrogen production equipment by ammonia decomposition under catalysis of plasma and metal oxide and experimental method | |
| CN104157889A (en) | Methanol steam reforming hydrogen production reactor for fuel cell car | |
| CN102802334A (en) | Sliding-arc-discharge plasma generation device loaded with magnetic field | |
| CN114843551A (en) | A kind of fuel processor and hydrogen production method | |
| CN201165470Y (en) | An efficient, fast and compact vehicle-mounted hydrogen-rich gas preparation device | |
| CN101457715A (en) | Mobile hydrogen making engine fuel system and device thereof | |
| WO2000026518A1 (en) | Plasmatron-catalyst system | |
| CN102020243A (en) | Method for decomposing water into hydrogen-oxygen mixed gas fuel | |
| CN201003443Y (en) | Diesel engine exhaust system with fuel reforming mechanism | |
| CN101368736A (en) | Method and device for promoting combustion | |
| Houseman et al. | Onboard hydrogen generation for automobiles | |
| CN101671004A (en) | Three-cavity series plasma vehicular hydrogen-rich gas generator | |
| CN103086324B (en) | Device and method for carrying out atomization and catalytic reforming on organic liquid fuels | |
| CN105655615A (en) | Methanol fuel battery system for automobile and working method of system | |
| CN109876751B (en) | A kind of plasma reactor and its application | |
| CN101293634A (en) | Compact type following hydrogen production plant | |
| CN215479718U (en) | Plasma fuel reforming hydrogen production device | |
| CN114768714A (en) | Non-thermal arc plasma liquid fuel gasification device and method for improving gasification efficiency | |
| CN114562394A (en) | Fuel direct-fired supply system for internal combustion engine | |
| Chao et al. | Onboard motorcycle plasma-assisted catalysis system–Role of plasma and operating strategy | |
| CN111342090B (en) | High-temperature fuel cell system | |
| CN222181819U (en) | Combustion catalytic reforming hydrogen production device | |
| RU110289U1 (en) | DEVICE FOR PRODUCING SYNTHESIS GAS |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20081217 Termination date: 20100924 |