CN210716927U - Mobile Hydrogenation Unit - Google Patents

Mobile Hydrogenation Unit Download PDF

Info

Publication number
CN210716927U
CN210716927U CN201920809580.7U CN201920809580U CN210716927U CN 210716927 U CN210716927 U CN 210716927U CN 201920809580 U CN201920809580 U CN 201920809580U CN 210716927 U CN210716927 U CN 210716927U
Authority
CN
China
Prior art keywords
gas
hydrogen
hydrogenation
storage tank
hydrogen production
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
Application number
CN201920809580.7U
Other languages
Chinese (zh)
Inventor
吴倩
叶联忠
黄湘集
李桓
吴婉怡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Guangdong Hongyuan Hydrogen Power Equipment Manufacturing Co ltd
Original Assignee
Guangdong Hongyuan Hydrogen Power Equipment Manufacturing Co ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangdong Hongyuan Hydrogen Power Equipment Manufacturing Co ltd filed Critical Guangdong Hongyuan Hydrogen Power Equipment Manufacturing Co ltd
Priority to CN201920809580.7U priority Critical patent/CN210716927U/en
Application granted granted Critical
Publication of CN210716927U publication Critical patent/CN210716927U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/32Hydrogen storage
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Hydrogen, Water And Hydrids (AREA)

Abstract

The utility model discloses a movable hydrogenation device, which comprises a hydrogen production device which can be arranged on a movable carrier, a gas storage tank and a hydrogenation device which is connected with the gas storage tank, wherein the hydrogen production device adopts normal-pressure metal-water reaction to produce hydrogen, and the gas storage tank is connected with the hydrogen production device and is used for temporarily storing the hydrogen generated in the hydrogen production device; the hydrogenation device is connected with the gas storage tank and is used for adding hydrogen to power equipment taking hydrogen as energy; by using the mobile hydrogenation device with the structure, the hydrogen production device can be moved to an area without a fixed hydrogenation station by the mobile carrier, so that the scale of the existing hydrogenation station is supplemented with less cost; in addition, the hydrogen production device adopts the metal-water reaction to produce hydrogen, so that a large amount of energy is not required to be consumed in hydrogen production and storage, and the hydrogen production and hydrogenation are realized in a real sense; moreover, the metal reaction fuel-aluminum is used, so that the hydrogen storage ratio is high, the energy density of unit volume is large, the metal reaction fuel-aluminum can be used while being used, and the volume of the gas storage tank can be effectively reduced.

Description

移动式加氢装置Mobile Hydrogenation Unit

技术领域technical field

本实用新型涉及移动加氢技术领域,尤其涉及一种采用金属-水反应实时制氢的移动式加氢装置。The utility model relates to the technical field of mobile hydrogenation, in particular to a mobile hydrogenation device which adopts metal-water reaction to produce hydrogen in real time.

背景技术Background technique

近年来,随着国家推动氢燃料电池汽车行业快速发展,与之配套的加氢站的完善速度远远无法跟上,氢能源车多、加氢站少、加氢难的问题日益突出,移动加氢站应运而生。移动加氢站现有技术方案有以下几种:1、使用电解水制氢,在该方案中,需要将生成的氢气高压存储到集装箱中,要达到该方按的制氢速率,至少需要一个MW级别变电站给集装箱供电,根本无法实现随时随地加氢,况且高压储氢运输存在安全隐患和高成本问题;2、在气源处使用储氢模块存储氢气,将制氢装置和压缩装置放在地面,把氢气的存储和加注装置放在车上,将装载高压氢气的瓶组进行运输,到特定的位置对氢燃料汽车进行加注。该方案始终脱离不了地面加氢站,运输过程安全隐患、高成本问题。3、使用甲醇制氢技术,却无氢气提纯装置,所产生的氢气浓度不能达到燃料电池汽车所需氢气浓度,另外不管使用何种技术重整甲醇制氢,其分解气中有大量的CO (30%以上)反应物存在有毒气体、存在安全隐患等问题。In recent years, as the country promotes the rapid development of the hydrogen fuel cell vehicle industry, the speed of improvement of the supporting hydrogen refueling stations is far from being able to keep up. The hydrogen refueling station came into being. The existing technical solutions for the mobile hydrogen refueling station are as follows: 1. Hydrogen production using electrolyzed water. In this solution, the generated hydrogen needs to be stored in a container under high pressure. To achieve the hydrogen production rate, at least one MW-level substations supply power to containers, and it is impossible to achieve hydrogen refueling anytime and anywhere. Moreover, high-pressure hydrogen storage transportation has potential safety hazards and high costs; 2. Use hydrogen storage modules at the gas source to store hydrogen, and place the hydrogen production device and compression device. On the ground, the hydrogen storage and filling device is placed on the vehicle, and the cylinder group loaded with high-pressure hydrogen is transported to a specific location to fill the hydrogen fuel vehicle. This solution has always been inseparable from the ground hydrogen refueling station, which has hidden safety hazards and high costs in the transportation process. 3. The methanol hydrogen production technology is used, but there is no hydrogen purification device, and the concentration of hydrogen produced cannot reach the hydrogen concentration required by the fuel cell vehicle. In addition, no matter what technology is used to reform methanol to produce hydrogen, there is a large amount of CO ( 30% or more) the reactants have problems such as toxic gas and potential safety hazards.

实用新型内容Utility model content

本实用新型的目的是为解决上述技术问题而提供一种可实现对氢气随用随制而且安全可靠的移动式加氢装置。The purpose of the utility model is to provide a safe and reliable mobile hydrogenation device that can realize the production of hydrogen on demand to solve the above technical problems.

为了实现上述目的,本实用新型公开了一种移动式加氢装置,其包括可安装在一移动载体上的制氢装置、储气罐以及与所述储气罐连接的加氢装置,所述制氢装置采用常压金属-水反应制氢,所述储气罐与所述制氢装置连接,用于暂存所述制氢装置中生成的氢气;所述加氢装置与所述储气罐连接,用于对以氢为能源的动力设备添加氢气。In order to achieve the above purpose, the utility model discloses a mobile hydrogenation device, which comprises a hydrogen production device which can be installed on a mobile carrier, a gas storage tank and a hydrogenation device connected with the gas storage tank. The hydrogen production device adopts atmospheric pressure metal-water reaction to produce hydrogen, the gas storage tank is connected with the hydrogen production device, and is used for temporarily storing the hydrogen generated in the hydrogen production device; the hydrogenation device is connected to the gas storage device. Tank connection for adding hydrogen to hydrogen-powered power equipment.

与现有技术相比,本实用新型移动式加氢装置,将制氢装置和储气罐安装在一移动载体上,可根据所需将加氢装置和储气罐安装到一移动载体,通过该移动载体将制氢装置移动到不具有固定式加氢站的区域,从而以较小的成本对现有加氢站的规模作以补充;另外,由于制氢装置采用金属-水反应制氢,与现有的电解水制氢相比,不依赖电网以及加氢站运行,不需要消耗大量的能源在制氢和储氢上,做到真正意义上的移动制氢加氢;再者,使用金属反应燃料,储氢比高,单位体积的能量密度大,可以边用边制,因此可有效缩减储气罐的体积,而且金属-水制氢系统的安全性和经济性都比较高,制氢过程不会产生有毒气体、不会产生高温(整个反应的温度在100℃以下),对环境友好且安全可靠。Compared with the prior art, the mobile hydrogenation device of the present utility model installs the hydrogen production device and the gas storage tank on a mobile carrier, and the hydrogenation device and the gas storage tank can be installed on a mobile carrier according to the requirements, The mobile carrier moves the hydrogen production device to an area without a fixed hydrogen refueling station, so as to supplement the scale of the existing hydrogen refueling station at a lower cost; in addition, since the hydrogen production device adopts the metal-water reaction to produce hydrogen , Compared with the existing hydrogen production by electrolysis of water, it does not rely on the power grid and hydrogen refueling stations to operate, and does not need to consume a lot of energy in hydrogen production and storage, so as to achieve mobile hydrogen production and hydrogenation in the true sense; Using metal reaction fuel, the hydrogen storage ratio is high, the energy density per unit volume is high, and it can be produced while using, so the volume of the gas storage tank can be effectively reduced, and the safety and economy of the metal-water hydrogen production system are relatively high. The hydrogen production process does not produce toxic gas or high temperature (the temperature of the entire reaction is below 100°C), which is environmentally friendly, safe and reliable.

较佳地,所述制氢装置包括反应釜、储水箱、加热缓存器、注水装置和输气管路;所述反应釜用于为铝-水反应制氢提供一反应容器,所述注水装置用于将所述储水箱内的水注入所述加热缓存器,所述加热缓存器用于将水加热到铝- 水反应所需的温度并输出给所述反应釜,所述输气管路的一端与所述反应釜的出气口连接,所述输气管路的另一端与所述储气罐连接。Preferably, the hydrogen production device includes a reaction kettle, a water storage tank, a heating buffer, a water injection device and a gas pipeline; the reaction kettle is used to provide a reaction vessel for hydrogen production by aluminum-water reaction, and the water injection device uses In order to inject the water in the water storage tank into the heating buffer, the heating buffer is used to heat the water to the temperature required for the aluminum-water reaction and output it to the reactor, and one end of the gas pipeline is connected to the heating buffer. The gas outlet of the reaction kettle is connected, and the other end of the gas transmission pipeline is connected with the gas storage tank.

较佳地,所述制氢装置还包括一设置在所述输气管路上用于对所述反应釜输出的氢气降温的降温装置。Preferably, the hydrogen production device further includes a cooling device arranged on the gas transmission pipeline for cooling the hydrogen output from the reactor.

较佳地,所述降温装置包括一换热器,所述换热器还通过一换热水泵与一风冷散热器连接。Preferably, the cooling device includes a heat exchanger, and the heat exchanger is also connected to an air-cooled radiator through a heat exchange water pump.

较佳地,所述输气管路上于所述换热器的后端还设置有一气液分离器和一干燥冷却器,所述气液分离器的进气端与所述换热器的出气端连接,所述气液分离器的出气端与所述干燥冷却器的进气端连接。Preferably, a gas-liquid separator and a drying cooler are also provided on the gas pipeline at the rear end of the heat exchanger, and the gas-liquid separator has an air inlet end and an air outlet end of the heat exchanger. connection, the gas outlet end of the gas-liquid separator is connected with the inlet end of the drying cooler.

较佳地,所述输气管路上于所述干燥冷却器的后端还设置一用于对所述氢气进行净化和脱水的分子筛。Preferably, a molecular sieve for purifying and dehydrating the hydrogen is further provided on the gas pipeline at the rear end of the drying cooler.

较佳地,所述加氢装置为一加氢枪,所述储气罐通过一加氢管路与所述加氢枪连接,所述加氢管路上设置有流量计和气体压缩器。Preferably, the hydrogenation device is a hydrogenation gun, the gas storage tank is connected to the hydrogenation gun through a hydrogenation pipeline, and a flowmeter and a gas compressor are arranged on the hydrogenation pipeline.

较佳地,所述气体压缩器包括串联在一起的一级压缩器和二级压缩器。Preferably, the gas compressor includes a primary compressor and a secondary compressor connected in series.

较佳地,所述移动载体上安装一可移动式的箱体,所述制氢装置和所述储气罐安装在所述箱体内,所述箱体上还设置一售气系统。Preferably, a movable box body is installed on the mobile carrier, the hydrogen production device and the gas storage tank are installed in the box body, and a gas sales system is also arranged on the box body.

较佳地,所述箱体内还安装一电源箱,所述电源箱内设置有可移动电源,所述可移动电源用于为所述制氢装置和所述售气系统提供电力供应。Preferably, a power supply box is also installed in the box, and a movable power supply is arranged in the power supply box, and the movable power supply is used to provide power supply for the hydrogen production device and the gas sales system.

附图说明Description of drawings

图1为本实用新型实施例移动式加氢装置的立体结构示意图。FIG. 1 is a schematic three-dimensional structure diagram of a mobile hydrogenation device according to an embodiment of the present invention.

图2为图1中位于箱体内部的制氢装置的立体结构示意图。FIG. 2 is a schematic three-dimensional structural diagram of the hydrogen production device located inside the box in FIG. 1 .

图3为本实用新型实施例中,储气罐与加气装置的连接结构示意图。FIG. 3 is a schematic diagram of the connection structure of the gas storage tank and the gas filling device in the embodiment of the present invention.

图4为图2中制氢装置的反应原理结构示意图。FIG. 4 is a schematic structural diagram of the reaction principle of the hydrogen production device in FIG. 2 .

具体实施方式Detailed ways

为详细说明本实用新型的技术内容、结构特征、实现原理及所实现目的及效果,以下结合实施方式并配合附图详予说明。In order to describe in detail the technical content, structural features, realization principle, realized objects and effects of the present invention, the following detailed description is given in conjunction with the embodiments and the accompanying drawings.

如图1至图3所示,本实用新型公开了一种移动式加氢装置,其包括可安装在一移动载体上的制氢装置2、储气罐3以及与储气罐3连接的加气装置4,制氢装置2采用常压金属-水反应制氢,储气罐3与制氢装置2连接,用于暂存制氢装置2中生成的氢气;加气装置4与储气罐3连接,用于对以氢为能源的动力设备添加氢气。本实施例中的移动载体可为手推车、三轮车、货车等,加气装置4为一加氢枪,通过该加氢枪对其他动力设备进行加氢操作。本实施例中的移动式加氢装置,可根据所需将加气装置4和储气罐3安装到一移动载体上,通过该移动载体将制氢装置2移动到不具有固定式加氢站的区域,从而以较小的成本对现有加氢站的规模作以补充;另外,由于制氢装置2采用金属-水反应制氢,与现有的电解水制氢相比,不依赖电网以及加氢站运行,不需要消耗大量的能源在制氢和储氢上,做到真正意义上的移动制氢加氢;再者,使用金属反应燃料,储氢比高,单位体积的能量密度大,可以边用边制,因此可有效缩减储气罐3的体积,而且金属-水制氢系统的安全性和经济性都比较高,制氢过程不会产生有毒气体、不会产生高温(整个反应的温度在100℃以下),对环境友好且安全可靠。As shown in FIG. 1 to FIG. 3 , the utility model discloses a mobile hydrogenation device, which includes a hydrogen production device 2 that can be installed on a mobile carrier, a gas storage tank 3 and a gas storage tank 3 connected to the gas tank. Gas device 4, hydrogen production device 2 adopts atmospheric pressure metal-water reaction to produce hydrogen, gas storage tank 3 is connected with hydrogen production device 2, and is used to temporarily store the hydrogen generated in hydrogen production device 2; gas filling device 4 and gas storage tank 3 connection for adding hydrogen to power equipment using hydrogen as energy. The mobile carrier in this embodiment can be a trolley, a tricycle, a truck, etc., and the gas charging device 4 is a hydrogen charging gun, through which the hydrogen charging operation is performed on other power equipment. In the mobile hydrogenation device in this embodiment, the gas filling device 4 and the gas storage tank 3 can be installed on a mobile carrier as required, and the hydrogen production device 2 can be moved to a place without a stationary hydrogenation station through the mobile carrier. In addition, since the hydrogen production unit 2 adopts the metal-water reaction to produce hydrogen, compared with the existing hydrogen production by electrolysis of water, it does not rely on the power grid. And the operation of the hydrogen refueling station does not need to consume a lot of energy in hydrogen production and hydrogen storage, so as to achieve mobile hydrogen production and hydrogenation in the true sense; in addition, using metal reaction fuel, the hydrogen storage ratio is high, and the energy density per unit volume is high. Large, can be produced while using, so the volume of the gas storage tank 3 can be effectively reduced, and the safety and economy of the metal-water hydrogen production system are relatively high, and the hydrogen production process will not produce toxic gas, no high temperature ( The temperature of the whole reaction is below 100°C), which is environmentally friendly and safe and reliable.

如图2和图4所示,制氢装置2为一常压铝-水反应制氢系统,其包括反应釜20、储水箱21、加热缓存器22、注水装置23和输气管路7。反应釜20用于为铝-水反应制氢提供一反应容器,注水装置23用于将储水箱21内的水注入加热缓存器22,加热缓存器22用于将水加热到铝-水反应所需的温度并输出给反应釜20,输气管路7的一端与反应釜20的出气口连接,输气管路7的另一端与储气罐3连接。当需要给以氢气为动力能源的设备供气时,控制注水装置23启动,将储水箱21中的水注入加热缓存器22,当加热缓存器22将水加热到所需温度时,输入到反应釜20内,反应釜20内的活性铝开始反应,生成氢气,氢气经由输气管路7输出给储气罐3。由于反应釜20中生成的氢气的温度比较高,较佳地,制氢装置2还包括一设置在输气管路7上用于对反应釜20输出的氢气降温的降温装置。本实施例中,该降温装置包括一换热器24,换热器24还通过一换热水泵25与一风冷散热器26连接。高温氢气通过换热器24后将氢气中的热量置换给换热器24中的冷却水7,冷却水升温。换热水泵25将换热器24中的热水抽入风冷散热器26,通过风冷散热器26将水中的热量散发到大气中,由于换热器24和风冷散热器26通过换热水泵25构成一个循环回路,因此冷却后的水又从风冷散热器26流回换热器24,从而实现冷却水的循环利用。本实施例中,注水装置23可通过换热器24与加热缓存器22连接,这样,从储水箱21 中抽出的冷水在换热器24中可吸收氢气的部分温度,而被加热,然后再注入加热缓存器22,从而充分利用换热器24中的废热。As shown in FIG. 2 and FIG. 4 , the hydrogen production device 2 is an atmospheric pressure aluminum-water reaction hydrogen production system, which includes a reactor 20 , a water storage tank 21 , a heating buffer 22 , a water injection device 23 and a gas pipeline 7 . The reaction kettle 20 is used to provide a reaction vessel for the aluminum-water reaction hydrogen production, and the water injection device 23 is used to inject the water in the water storage tank 21 into the heating buffer 22, and the heating buffer 22 is used to heat the water to the aluminum-water reaction chamber. The required temperature is output to the reaction kettle 20, one end of the gas pipeline 7 is connected to the gas outlet of the reactor 20, and the other end of the gas pipeline 7 is connected to the gas storage tank 3. When it is necessary to supply gas to the equipment using hydrogen as the power source, the water injection device 23 is controlled to start, and the water in the water storage tank 21 is injected into the heating buffer 22. When the heating buffer 22 heats the water to the required temperature, it is input to the reaction In the kettle 20 , the active aluminum in the reaction kettle 20 starts to react to generate hydrogen, and the hydrogen is output to the gas storage tank 3 through the gas transmission pipeline 7 . Since the temperature of the hydrogen generated in the reaction kettle 20 is relatively high, preferably, the hydrogen production device 2 further includes a cooling device arranged on the gas transmission pipeline 7 for cooling the hydrogen output from the reaction kettle 20 . In this embodiment, the cooling device includes a heat exchanger 24 , and the heat exchanger 24 is also connected to an air-cooled radiator 26 through a heat exchange water pump 25 . After the high-temperature hydrogen passes through the heat exchanger 24, the heat in the hydrogen is replaced with the cooling water 7 in the heat exchanger 24, and the cooling water is heated up. The heat exchange water pump 25 pumps the hot water in the heat exchanger 24 into the air-cooled radiator 26, and the air-cooled radiator 26 dissipates the heat in the water to the atmosphere. The water pump 25 forms a circulation loop, so the cooled water flows from the air-cooled radiator 26 back to the heat exchanger 24, thereby realizing the circulation of the cooling water. In this embodiment, the water injection device 23 can be connected to the heating buffer 22 through the heat exchanger 24, so that the cold water drawn from the water storage tank 21 can absorb part of the temperature of the hydrogen in the heat exchanger 24 to be heated, and then be heated again. Injecting into the heating buffer 22 to fully utilize the waste heat in the heat exchanger 24 .

进一步地,输气管路7上于换热器24的后端还设置有一气液分离器27和一干燥冷却器28,气液分离器27的进气端与换热器24的出气端连接,气液分离器27的出气端与干燥冷却器28的进气端连接。氢气经过换热器24,由于还含有水分,因此,通过气液分离器27将氢气中的大部分水分分离出来,然后经过干燥冷却器28对氢气进一步的干燥和冷却,从而提高氢气的质量。另外气液分离器27还可通过管路与储水箱21连接,将分离出的水回流到储水箱21中,达到节约用水的目的。较佳地,输气管路7上于干燥冷却器28的后端还设置一用于对氢气进行净化和脱水的分子筛29,通过该分子筛29,除去氢气中的废气和水分子,以对输出到储气罐3中的氢气进一步净化。Further, a gas-liquid separator 27 and a drying cooler 28 are also provided on the gas pipeline 7 at the rear end of the heat exchanger 24. The air inlet end of the gas-liquid separator 27 is connected to the air outlet end of the heat exchanger 24, The outlet end of the gas-liquid separator 27 is connected to the inlet end of the drying cooler 28 . The hydrogen passes through the heat exchanger 24. Since it also contains moisture, most of the moisture in the hydrogen is separated by the gas-liquid separator 27, and then the hydrogen is further dried and cooled through the drying cooler 28, thereby improving the quality of the hydrogen. In addition, the gas-liquid separator 27 can also be connected to the water storage tank 21 through a pipeline, and the separated water is returned to the water storage tank 21 to achieve the purpose of saving water. Preferably, a molecular sieve 29 for purifying and dehydrating hydrogen is also provided on the gas pipeline 7 at the rear end of the drying cooler 28, and through the molecular sieve 29, the waste gas and water molecules in the hydrogen are removed, so that the output gas and water molecules are removed. The hydrogen in the gas storage tank 3 is further purified.

本实用新型移动式加氢装置另一较佳实施例中,储气罐3通过一加氢管路 50与一加氢枪连接,加氢管路50上设置有流量计51和气体压缩器。通过加氢枪可方便加氢,在加氢过程中,通过流量计51的变化可方便控制加氢量。由于在加气过程中,受气设备上的气压越来越高,因此,通过气体压缩器,可有效提高加气速度和加气压强。本实施例中,气体压缩器包括串联在一起的一级压缩器52和二级压缩器53。另外,为便于对储气罐3输出的氢气进行压缩,加氢管路50上还可设置一冷却模块54。In another preferred embodiment of the mobile hydrogenation device of the present invention, the gas storage tank 3 is connected with a hydrogenation gun through a hydrogenation pipeline 50, and a flowmeter 51 and a gas compressor are arranged on the hydrogenation pipeline 50. Hydrogenation can be facilitated by the hydrogenation gun, and the hydrogenation amount can be conveniently controlled by changing the flow meter 51 during the hydrogenation process. Since the gas pressure on the gas receiving equipment is getting higher and higher during the gas filling process, the gas compressor can effectively increase the gas filling speed and the gas pressure. In this embodiment, the gas compressor includes a primary compressor 52 and a secondary compressor 53 that are connected in series. In addition, in order to facilitate the compression of the hydrogen output from the gas storage tank 3 , a cooling module 54 may also be provided on the hydrogenation pipeline 50 .

如图1,为方便移放制氢装置2,移动载体上可安装一可移动式的箱体1,制氢装置2和储气罐3安装在箱体1内,箱体1上安装一售气系统,以方便售卖氢气。另外,箱体1内还安装一电源箱6,电源箱6内设置有可移动电源,可移动电源用于为制氢装置2的启动和售气系统提供电力供应。本实施例中的售气系统包括安装在箱体1上的显示屏10,以显示加气量、价格和金额等。As shown in Figure 1, in order to facilitate the removal of the hydrogen production device 2, a movable box body 1 can be installed on the mobile carrier. The hydrogen production device 2 and the gas storage tank 3 are installed in the box body 1. gas system to facilitate the sale of hydrogen. In addition, a power supply box 6 is also installed in the box body 1, and a movable power supply is arranged in the power supply box 6, and the movable power supply is used to provide power supply for the startup of the hydrogen production device 2 and the gas sales system. The gas vending system in this embodiment includes a display screen 10 installed on the box body 1 to display the gas filling amount, price and amount, and the like.

以上所揭露的仅为本实用新型的较佳实例而已,当然不能以此来限定本实用新型之权利范围,因此依本实用新型申请专利范围所作的等同变化,仍属于本实用新型所涵盖的范围。What has been disclosed above is only a preferred example of the present invention, of course, it cannot limit the scope of rights of the present invention. Therefore, the equivalent changes made according to the scope of the patent application of the present invention still belong to the scope covered by the present invention. .

Claims (10)

1.一种移动式加氢装置,其特征在于,包括可安装在一移动载体上的制氢装置、储气罐以及与所述储气罐连接的加氢装置,所述制氢装置采用常压金属-水反应制氢,所述储气罐与所述制氢装置连接,用于暂存所述制氢装置中生成的氢气;所述加氢装置与所述储气罐连接,用于对以氢为能源的动力设备添加氢气。1. a mobile hydrogenation unit, is characterized in that, comprises the hydrogenation unit that can be installed on a mobile carrier, the gas storage tank and the hydrogenation unit connected with the gas storage tank, and the hydrogenation unit adopts a conventional hydrogenation unit. Press metal-water reaction to produce hydrogen, the gas storage tank is connected with the hydrogen production device, and is used for temporarily storing the hydrogen generated in the hydrogen production device; the hydrogenation device is connected with the gas storage tank, used for Add hydrogen to power equipment powered by hydrogen. 2.根据权利要求1所述的移动式加氢装置,其特征在于,所述制氢装置包括反应釜、储水箱、加热缓存器、注水装置和输气管路;所述反应釜用于为铝-水反应制氢提供一反应容器,所述注水装置用于将所述储水箱内的水注入所述加热缓存器,所述加热缓存器用于将水加热到铝-水反应所需的温度并输出给所述反应釜,所述输气管路的一端与所述反应釜的出气口连接,所述输气管路的另一端与所述储气罐连接。2. The mobile hydrogenation device according to claim 1, wherein the hydrogen production device comprises a reactor, a water storage tank, a heating buffer, a water injection device and a gas pipeline; the reactor is used for aluminum -Hydrogen production by water reaction provides a reaction vessel, and the water injection device is used to inject the water in the water storage tank into the heating buffer, and the heating buffer is used to heat the water to the temperature required for the aluminum-water reaction and output to the reaction kettle, one end of the gas transmission pipeline is connected to the gas outlet of the reaction kettle, and the other end of the gas transmission pipeline is connected to the gas storage tank. 3.根据权利要求2所述的移动式加氢装置,其特征在于,所述制氢装置还包括一设置在所述输气管路上用于对所述反应釜输出的氢气降温的降温装置。3 . The mobile hydrogenation device according to claim 2 , wherein the hydrogen production device further comprises a cooling device arranged on the gas transmission pipeline for cooling the hydrogen output from the reactor. 4 . 4.根据权利要求3所述的移动式加氢装置,其特征在于,所述降温装置包括一换热器,所述换热器还通过一换热水泵与一风冷散热器连接。4 . The mobile hydrogenation device according to claim 3 , wherein the cooling device comprises a heat exchanger, and the heat exchanger is also connected to an air-cooled radiator through a heat exchange water pump. 5 . 5.根据权利要求4所述的移动式加氢装置,其特征在于,所述输气管路上于所述换热器的后端还设置有一气液分离器和一干燥冷却器,所述气液分离器的进气端与所述换热器的出气端连接,所述气液分离器的出气端与所述干燥冷却器的进气端连接。5. The mobile hydrogenation device according to claim 4, characterized in that, a gas-liquid separator and a drying cooler are also provided at the rear end of the heat exchanger on the gas pipeline, and the gas-liquid The air inlet end of the separator is connected with the air outlet end of the heat exchanger, and the air outlet end of the gas-liquid separator is connected with the air inlet end of the drying cooler. 6.根据权利要求5所述的移动式加氢装置,其特征在于,所述输气管路上于所述干燥冷却器的后端还设置一用于对所述氢气进行净化和脱水的分子筛。6 . The mobile hydrogenation device according to claim 5 , wherein a molecular sieve for purifying and dehydrating the hydrogen gas is further provided at the rear end of the drying cooler on the gas pipeline. 7 . 7.根据权利要求1所述的移动式加氢装置,其特征在于,所述加氢装置为一加氢枪,所述储气罐通过一加氢管路与所述加氢枪连接,所述加氢管路上设置有流量计和气体压缩器。7. The mobile hydrogenation device according to claim 1, wherein the hydrogenation device is a hydrogenation gun, and the gas storage tank is connected with the hydrogenation gun through a hydrogenation pipeline, so that the The hydrogenation pipeline is provided with a flow meter and a gas compressor. 8.根据权利要求7所述的移动式加氢装置,其特征在于,所述气体压缩器包括串联在一起的一级压缩器和二级压缩器。8. The mobile hydrogenation unit according to claim 7, wherein the gas compressor comprises a primary compressor and a secondary compressor connected in series. 9.根据权利要求1所述的移动式加氢装置,其特征在于,所述移动载体上安装一可移动式的箱体,所述制氢装置和所述储气罐安装在所述箱体内,所述箱体上还设置一售气系统。9 . The mobile hydrogenation device according to claim 1 , wherein a movable box is installed on the mobile carrier, and the hydrogen production device and the gas storage tank are installed in the box. 10 . , and a gas sales system is also set on the box body. 10.根据权利要求9所述的移动式加氢装置,其特征在于,所述箱体内还安装一电源箱,所述电源箱内设置有可移动电源,所述可移动电源用于为所述制氢装置和所述售气系统提供电力供应。10. The mobile hydrogenation device according to claim 9, wherein a power supply box is further installed in the box, and a movable power supply is arranged in the power supply box, and the movable power supply is used for the The hydrogen production unit and the gas sales system provide power supply.
CN201920809580.7U 2019-05-30 2019-05-30 Mobile Hydrogenation Unit Expired - Fee Related CN210716927U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920809580.7U CN210716927U (en) 2019-05-30 2019-05-30 Mobile Hydrogenation Unit

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920809580.7U CN210716927U (en) 2019-05-30 2019-05-30 Mobile Hydrogenation Unit

Publications (1)

Publication Number Publication Date
CN210716927U true CN210716927U (en) 2020-06-09

Family

ID=70964422

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920809580.7U Expired - Fee Related CN210716927U (en) 2019-05-30 2019-05-30 Mobile Hydrogenation Unit

Country Status (1)

Country Link
CN (1) CN210716927U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112624042A (en) * 2020-12-16 2021-04-09 浙江高成绿能科技有限公司 Chemical hydrogen production system and hydrogen production method
CN113188037A (en) * 2021-05-25 2021-07-30 王广武 Low-pressure hydrogen storage station and hydrogen injection, hydrogen transportation, hydrogen storage and hydrogen supply method
CN113606499A (en) * 2021-08-13 2021-11-05 上海氢枫能源技术有限公司 Water chilling unit suitable for hydrogen filling station and use method thereof
CN113915525A (en) * 2021-10-29 2022-01-11 江苏氢枫能源装备有限公司 Solid hydrogen-storing hydrogen adsorbing and releasing device

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112624042A (en) * 2020-12-16 2021-04-09 浙江高成绿能科技有限公司 Chemical hydrogen production system and hydrogen production method
CN113188037A (en) * 2021-05-25 2021-07-30 王广武 Low-pressure hydrogen storage station and hydrogen injection, hydrogen transportation, hydrogen storage and hydrogen supply method
CN113606499A (en) * 2021-08-13 2021-11-05 上海氢枫能源技术有限公司 Water chilling unit suitable for hydrogen filling station and use method thereof
CN113915525A (en) * 2021-10-29 2022-01-11 江苏氢枫能源装备有限公司 Solid hydrogen-storing hydrogen adsorbing and releasing device
CN113915525B (en) * 2021-10-29 2022-08-23 江苏氢枫能源装备有限公司 Solid hydrogen-storing hydrogen adsorbing and releasing device

Similar Documents

Publication Publication Date Title
CN210716927U (en) Mobile Hydrogenation Unit
Rong et al. Techno-economic analysis of hydrogen storage and transportation from hydrogen plant to terminal refueling station
Liu et al. Development of a gaseous and solid-state hybrid system for stationary hydrogen energy storage
CN217736920U (en) Liquid hydrogen vaporization hydrogenation system
US9580308B2 (en) Storing and transporting energy
CN209691855U (en) Vehicle-mounted fuel cell system and hydrogen-powered vehicle
CN103185196A (en) Metal hydride hydrogen storage system and manufacture method thereof
CN102167285A (en) Portable, safe and controllable hydrolysis hydrogen-producing device
CN110137534A (en) Fuel cell system and hydrogen-powered vehicle
CN110217755B (en) Liquid hydrogen storage carrier hydrogenation system
CN210595250U (en) Hydrogenation system for liquid hydrogen storage carrier
CN117366465A (en) Hydrogenation integrated system based on organic liquid hydrogen storage
Koh et al. Hydrogen generation system for fuel cells based on high pressure hydrolysis of solid-state sodium borohydride
CN103759135A (en) BOG (Boil Off Gas)-zero emission LNG (Liquefied Natural Gas) storage method and device
WO2023115622A1 (en) Catalytic combustion hydrogen storage and release device and method
CN218599448U (en) Mixed filling system for hydrogenation station
CN108469196B (en) High-temperature gas waste heat utilization system
CN116591868A (en) Hydrogen storage and supply system for marine engine
CN201946692U (en) Automobile-used hydrogen fuel cool refueling device
Jiang Expediting the innovation and application of solid hydrogen storage technology
CN114673930B (en) Energy-saving alloy hydrogen storage tank hydrogen charging system
CN205014038U (en) LNG gasification cold energy is retrieved and traditional cooling cooling tower combination system
CN110131573B (en) Quick filling system of hydrogen storage cylinder of hydrogen fuel cell automobile
CN216129329U (en) Skid-mounted methanol multiphase high-pressure hydrogen production and purification system
CN110416572A (en) A kind of heating system and method using fuel cell waste-heat formic acid reactor

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20200609