CN112251765B - A lead net-based water splitting hydrogen production device and its preparation method and use method - Google Patents

A lead net-based water splitting hydrogen production device and its preparation method and use method Download PDF

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CN112251765B
CN112251765B CN202011188670.2A CN202011188670A CN112251765B CN 112251765 B CN112251765 B CN 112251765B CN 202011188670 A CN202011188670 A CN 202011188670A CN 112251765 B CN112251765 B CN 112251765B
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anode
lead
cathode
hydrogen production
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CN112251765A (en
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康帅
陆文强
薛凤娟
付勰
王亮
冯双龙
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Chongqing Institute of Green and Intelligent Technology of CAS
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    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
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    • 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

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Abstract

The invention discloses a lead mesh-based water-splitting hydrogen production device, a preparation method and a use method thereof. The invention provides a method for preparing an anode of a high-efficiency PEM hydrolysis device by using non-noble metals, which has simple system structure and low price; and the anode based on the lead net can stabilize electrochemical hydrolysis reaction under acidic and high temperature (above 60 ℃).

Description

一种基于铅网的水分解制氢装置及其制备方法和使用方法A lead net-based water splitting hydrogen production device and its preparation method and use method

技术领域technical field

本发明属于电源技术领域,具体涉及一种基于铅网的水分解制氢装置及其制备方法和使用方法。The invention belongs to the technical field of power supplies, and in particular relates to a water splitting hydrogen production device based on lead grids, a preparation method and a use method thereof.

背景技术Background technique

氢气是能量密度最高的物质,可达33.3 kWh/kg,被当作一种二次能源载体,例如可作为火箭燃料。氢元素广泛存在于碳氢化物和水中,是地球上储量最大的元素之一。化石能源重整时会产生大量氢气作为副产物,与此相比,电解水制氢量可忽略。但清洁能源如风能、太阳能可通过电化学反应水解制备高纯度氢气,因此成为非常热门的制氢技术。目前碱性水解装置制氢占主导,然而酸性质子交换膜(PEM)水解装置具有反应快、节能、高集成等优点,因此也得到重视。Hydrogen is the substance with the highest energy density, up to 33.3 kWh/kg, and is used as a secondary energy carrier, for example as rocket fuel. Hydrogen widely exists in hydrocarbons and water, and is one of the most abundant elements on earth. When fossil energy is reformed, a large amount of hydrogen is produced as a by-product. Compared with this, the amount of hydrogen produced by electrolysis of water is negligible. However, clean energy such as wind energy and solar energy can produce high-purity hydrogen through electrochemical reaction hydrolysis, so it has become a very popular hydrogen production technology. At present, hydrogen production by alkaline hydrolysis devices is dominant, but acidic proton exchange membrane (PEM) hydrolysis devices have the advantages of fast response, energy saving, and high integration, so they have also received attention.

目前适用于PEM水解装置的电极主要是贵金属电极,如铂、氧化铂或铂合金作为阴极,钌、铷或其氧化物、合金作为阳极。贵金属储量贫乏、价格贵造成PEM水解装置极高的成本。而非贵金属材料或其化合物,尤其是过渡金属材料或其化合物,在酸性中极不稳定,在高温水解过程中制氢效率迅速衰减。At present, the electrodes suitable for PEM hydrolysis devices are mainly noble metal electrodes, such as platinum, platinum oxide or platinum alloys as cathodes, and ruthenium, rubidium or their oxides and alloys as anodes. The scarcity and high price of precious metals lead to the extremely high cost of the PEM hydrolysis device. Non-noble metal materials or their compounds, especially transition metal materials or their compounds, are extremely unstable in acid, and their hydrogen production efficiency decays rapidly during high-temperature hydrolysis.

发明内容Contents of the invention

基于现有技术中存在的问题,本发明提供一种基于铅网的水分解制氢装置及其制备方法和使用方法,本发明既可以通过加工铅金属网格,也可以在铅金属网格上生长低维氧化铅片,作为PEM水解装置阳极。并且在本发明中,没有使用贵金属,就可以实现在高温60℃下稳定水解制氢工艺,提高制氢效率且降低成本。Based on the problems existing in the prior art, the present invention provides a water splitting hydrogen production device based on lead grid and its preparation method and use method. A low-dimensional lead oxide sheet is grown to serve as the anode of the PEM hydrolysis device. Moreover, in the present invention, without using precious metals, a stable hydrolysis hydrogen production process can be realized at a high temperature of 60° C., improving hydrogen production efficiency and reducing costs.

依据本发明技术方案的第一方面,提出一种基于铅网的水分解制氢装置,其包括阳极、阴极和隔膜,其使用铅网或者氧化铅薄片覆盖的铅网作为阳极,使用热压铂碳PEM或者镀铂铅网或钛网或合金网作为阴极,使用PEM作为隔膜。According to the first aspect of the technical solution of the present invention, a water splitting hydrogen production device based on a lead grid is proposed, which includes an anode, a cathode and a diaphragm, which uses a lead grid or a lead grid covered with lead oxide flakes as an anode, and uses a hot-pressed platinum Carbon PEM or platinum-coated lead mesh or titanium mesh or alloy mesh is used as cathode, and PEM is used as separator.

其中,阳极、隔膜和阴极依序叠置构成水分解制氢装置主体。在阳极的延伸段和阴极的延伸段分别设置有直流电源接口。Among them, the anode, diaphragm and cathode are stacked in sequence to form the main body of the water splitting hydrogen production device. The extension section of the anode and the extension section of the cathode are respectively provided with DC power interfaces.

优选地,质子交换膜(PEM)为全氟磺酸型质子交换膜、Nafion重铸膜、非氟聚合物质子交换膜或新型复合质子交换膜。阳极使用网格材质,阳极为铅金属、合金或镀铂、钛、氧化锌、氧化钛的复合金属网。Preferably, the proton exchange membrane (PEM) is a perfluorosulfonic acid type proton exchange membrane, a Nafion recast membrane, a non-fluoropolymer proton exchange membrane or a new composite proton exchange membrane. The anode is made of grid material, and the anode is a composite metal mesh of lead metal, alloy or platinum-plated, titanium, zinc oxide, or titanium oxide.

依据本发明技术方案的第二方面,提出基于铅网的水分解制氢装置的制备方法,所述方法包括以下步骤。According to the second aspect of the technical solution of the present invention, a method for preparing a lead grid-based water splitting hydrogen production device is proposed, and the method includes the following steps.

步骤1,制备阳极铅网;采购铅箔,并用开孔机或者激光雕刻机在铅箔上开孔,制备成铅网用做阳极。Step 1, prepare anode lead mesh; purchase lead foil, and use a hole punching machine or a laser engraving machine to drill holes in the lead foil to prepare a lead mesh for use as an anode.

步骤2,制备阴极,用溅射镀膜机在铅箔上镀一层纳米铂金直接用作阴极。Step 2, prepare the cathode, and use a sputter coater to coat a layer of nano-platinum gold on the lead foil and use it directly as the cathode.

步骤3,将质子交换膜隔置在阳极和阴极中间,并用外壳保护层和固定夹夹紧上述阳极-隔膜-阴极,制备成了基于铅网的水分解制氢装置。In step 3, the proton exchange membrane is interposed between the anode and the cathode, and the above anode-diaphragm-cathode is clamped with the shell protective layer and the fixing clip, and a water splitting hydrogen production device based on lead mesh is prepared.

进一步地,所述步骤1使用溅射镀膜机在铅箔上镀一层纳米铂金直接用作阳极。Further, in step 1, a sputter coater is used to coat a layer of nano-platinum gold on the lead foil directly as an anode.

更进一步地,所述步骤1把铅网放在装有浓氨水的聚四氟乙烯杯里,在180℃高温高压反应6小时到72小时,在铅网上生长一层氧化铅片用作阳极。Further, in step 1, put the lead grid in a polytetrafluoroethylene cup filled with concentrated ammonia water, react under high temperature and high pressure at 180°C for 6 hours to 72 hours, and grow a layer of lead oxide sheet on the lead grid as an anode.

进一步地,所述步骤2直接制作质子交换膜(PEM)燃料电池阳极用的铂碳PEM膜作为阴极和制氢装置的隔膜。Further, the step 2 directly manufactures the platinum carbon PEM membrane for the anode of the proton exchange membrane (PEM) fuel cell as the cathode and the diaphragm of the hydrogen production device.

依据本发明技术方案的第三方面,提出一种基于铅网的水分解制氢装置的使用方法,其包括以下步骤。According to the third aspect of the technical solution of the present invention, a method for using a lead grid-based water splitting hydrogen production device is proposed, which includes the following steps.

步骤1,将直流电源接口与直流电源相连接,且阳极与电源正极相连,阴极与电源负极相连。Step 1, connect the DC power interface to the DC power supply, and connect the anode to the positive pole of the power supply, and connect the cathode to the negative pole of the power supply.

步骤2,将基于铅网的水分解制氢装置置于酸性水溶液中,将直流电源接口设置在液面上,且避免线路与水溶液相接触。Step 2, place the water splitting hydrogen production device based on the lead grid in the acidic aqueous solution, set the DC power interface on the liquid surface, and avoid the contact between the circuit and the aqueous solution.

步骤3,打开电源开关,从2 V开始缓慢升高电压,根据氢气的需求量调整到合适的电压,如氢气需求量大则电压高,氢气需求量小则电压低。Step 3. Turn on the power switch, slowly increase the voltage from 2 V, and adjust to an appropriate voltage according to the hydrogen demand. If the hydrogen demand is large, the voltage will be high, and if the hydrogen demand is small, the voltage will be low.

步骤4,气体制备完成后,先把直流电源调整到低电压,然后关闭直流电源,最后断开直流电源接口与直流电源的连接。Step 4: After the gas preparation is completed, first adjust the DC power supply to a low voltage, then turn off the DC power supply, and finally disconnect the DC power supply interface from the DC power supply.

与现有技术相比,本发明具有以下有益效果。Compared with the prior art, the present invention has the following beneficial effects.

第一,本发明提出了一种用非贵金属制备高效PEM水解装置阳极的方法,系统构造简单、价格便宜。First, the present invention proposes a method for preparing an anode of a high-efficiency PEM hydrolysis device with a non-noble metal, and the system structure is simple and the price is cheap.

第二,本发明提出的基于铅网的阳极能够在酸性和高温下(60 ℃以上)电化学水解反应稳定。Second, the lead grid-based anode proposed by the present invention is stable in electrochemical hydrolysis reaction under acidic and high temperature (above 60 °C).

附图说明Description of drawings

图1是依据本发明的基于铅网的水分解制氢装置示意图。Fig. 1 is a schematic diagram of a water splitting hydrogen production device based on a lead grid according to the present invention.

图2是依据本发明的阳极的结构示意图。Fig. 2 is a schematic diagram of the structure of the anode according to the present invention.

图3-1是依据本发明的阴极的结构示意图。Fig. 3-1 is a schematic diagram of the structure of the cathode according to the present invention.

图3-2是依据本发明的制膜工艺示意图。Fig. 3-2 is a schematic diagram of the film-making process according to the present invention.

图4-1为依据本发明的所示的阳极的照片。Figure 4-1 is a photograph of the anode shown in accordance with the present invention.

图4-2依据本发明的扫描电镜图。Fig. 4-2 is a scanning electron micrograph according to the present invention.

图5是依据本发明的阳极的水解性能曲线。Fig. 5 is a hydrolysis performance curve of an anode according to the present invention.

图6是依据本发明的制氢装置性能曲线。Fig. 6 is a performance curve of a hydrogen production device according to the present invention.

其中附图标记:“1”指示“阳极”,“2”指示“阴极”、“3”指示“PEM”,“4”指示“直流电源接口”。Wherein reference numerals: "1" indicates "anode", "2" indicates "cathode", "3" indicates "PEM", and "4" indicates "DC power interface".

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述。显然,所描述的实施例仅仅是本发明的一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。另外地,不应当将本发明的保护范围仅仅限制至下述具体实验方法或具体参数。The following will clearly and completely describe the technical solutions in the embodiments of the present invention with reference to the drawings in the embodiments of the present invention. Apparently, the described embodiments are only some of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without making creative efforts belong to the protection scope of the present invention. Additionally, the protection scope of the present invention should not be limited only to the specific experimental methods or specific parameters described below.

本发明从铅基材料在酸性中的稳定性出发,设计了一种基于铅网的水分解制氢装置,其中使用铅网或者氧化铅薄片覆盖的铅网作为阳极,使用热压铂碳PEM或者镀铂铅网(钛网或者合金网)作为阴极,使用PEM作为隔膜。本发明通过加工铅金属网格,也可以在铅金属网格上生长低维氧化铅片,作为PEM水解装置阳极,可达到高温60 ℃下稳定水解制氢的目的,提高制氢效率且降低成本。在本发明中没有使用贵金属。Starting from the stability of lead-based materials in acid, the present invention designs a water splitting hydrogen production device based on lead grids, in which lead grids or lead grids covered with lead oxide flakes are used as anodes, and hot-pressed platinum carbon PEM or Platinum-coated lead mesh (titanium mesh or alloy mesh) is used as the cathode, and PEM is used as the diaphragm. The invention can also grow low-dimensional lead oxide sheets on the lead metal grid by processing the lead metal grid, as the anode of the PEM hydrolysis device, which can achieve the purpose of stable hydrolysis hydrogen production at a high temperature of 60 °C, improve hydrogen production efficiency and reduce costs . Noble metals are used in the present invention.

如图1所示的基于铅网的水分解制氢装置,其包括阳极1、阴极2和隔膜3,隔膜优选使用PEM ,其中以阳极1、隔膜3和阴极2依序叠置构成水分解制氢装置主体,在阳极1的延伸段和阴极2的延伸段分别设置有直流电源接口4。在制氢过程中,直流电源通过直流电源接口4与装置接通,电源负极中流出的电子通过阴极2流入电解液,同时在阴极表面发生还原反应,阴极附近的电解液的氢离子得电子生成氢气;电源正极中流出的空穴通过阳极1流入电解液,同时在阳极电极表面发生氧化反应,阳极附近的电解液中的氢氧根离子失电子产生氧气。此外,在制氢过程中,电源中的电子通过阴极2流入电解液,在阴极电极表面产生氢气。As shown in Figure 1, the water splitting hydrogen production device based on lead mesh includes an anode 1, a cathode 2 and a diaphragm 3, and the diaphragm is preferably PEM, wherein the anode 1, diaphragm 3 and cathode 2 are stacked in sequence to form a water splitting system. The main body of the hydrogen device is provided with a DC power interface 4 on the extension section of the anode 1 and the extension section of the cathode 2 respectively. During the hydrogen production process, the DC power supply is connected to the device through the DC power supply interface 4, and the electrons flowing out of the negative electrode of the power supply flow into the electrolyte through the cathode 2, and at the same time, a reduction reaction occurs on the surface of the cathode, and hydrogen ions in the electrolyte near the cathode are generated by electrons. Hydrogen; holes flowing out of the positive electrode of the power supply flow into the electrolyte through the anode 1, and an oxidation reaction occurs on the surface of the anode electrode at the same time, and the hydroxide ions in the electrolyte near the anode lose electrons to generate oxygen. In addition, during the hydrogen production process, the electrons in the power supply flow into the electrolyte through the cathode 2, and hydrogen gas is generated on the surface of the cathode electrode.

其化学反应式如下。Its chemical reaction formula is as follows.

阳极:2H2O=O2↑+4H++4e-Anode: 2H 2 O=O 2 ↑+4H + +4e-

阴极:4H++4e-=2H2Cathode: 4H + +4e-=2H 2

总反应式:2H2O = H2↑+O2Overall reaction formula: 2H 2 O = H 2 ↑+O 2

根据法拉第电解定律,气体产量与电流成正比。According to Faraday's law of electrolysis, the gas production is proportional to the current.

作为隔膜的PEM(质子交换膜),优选满足以下条件的质子交换膜:良好的质子电导率、水分子在膜中的电渗透作用小、气体在膜中的渗透性尽可能小、电化学稳定性好、干湿转换性能好、具有一定的机械强度、可加工性好。质子交换膜(PEM)与一般化学电源中使用的隔膜有差异,推荐使用全氟磺酸型质子交换膜、Nafion重铸膜、非氟聚合物质子交换膜、新型复合质子交换膜等等。在本发明中,阴极和阳极用PEM隔开,避免阳极和阴极接触直接进行电子传输。As the PEM (proton exchange membrane) of the diaphragm, the proton exchange membrane that meets the following conditions is preferred: good proton conductivity, small electroosmosis of water molecules in the membrane, as little gas permeability in the membrane as possible, and electrochemical stability Good performance, good dry-wet conversion performance, certain mechanical strength, good processability. Proton exchange membrane (PEM) is different from the diaphragm used in general chemical power sources. It is recommended to use perfluorosulfonic acid type proton exchange membrane, Nafion recast membrane, non-fluoropolymer proton exchange membrane, new composite proton exchange membrane, etc. In the present invention, the cathode and the anode are separated by PEM, so as to avoid direct electron transmission between the anode and the cathode.

在本发明的基于铅网的水分解制氢装置中,直流电源接口4产生的1.5 V-5 V直流电压。In the lead grid-based water splitting hydrogen production device of the present invention, the DC power interface 4 generates a DC voltage of 1.5 V-5 V.

如图2所示阳极结构,阳极使用网格材质,优选是铅金属、合金或镀其他材料(如铂、钛、氧化锌、氧化钛等)的复合金属网(如图2上)。极片大小与氢气需求量正相关,即极片越大单位时间内同一电压/电流下制备的氢气量越多。在工作过程中,电解液中的电子通过该极流入电源,在电极表面产生氧气。阳极的微观部分优选是原位生长有氧化铅片的分层结构(如图2下)。网格形貌一方面增加了电化学反应面积,有利于气体的制备;另一方面,孔道有利于气体的扩散。The anode structure is shown in Figure 2. The anode is made of mesh material, preferably lead metal, alloy or composite metal mesh plated with other materials (such as platinum, titanium, zinc oxide, titanium oxide, etc.) (as shown in Figure 2). The size of the pole piece is positively correlated with the hydrogen demand, that is, the larger the pole piece is, the more hydrogen can be produced under the same voltage/current per unit time. During the working process, the electrons in the electrolyte flow into the power supply through the electrode, and oxygen is generated on the surface of the electrode. The microscopic part of the anode is preferably a layered structure with lead oxide sheets grown in situ (as shown in Figure 2 below). On the one hand, the grid morphology increases the electrochemical reaction area, which is beneficial to the preparation of gas; on the other hand, the pores are conducive to the diffusion of gas.

如图3-1所示的阴极结构,阴极主要活性材料是铂金属。阴极结构优选可以是网格状,如图3-1所示的铂金属镀在铅网、钛网或者合金网上,这样的网格形貌一方面增加了电化学反应面积,有利于气体的制备;另一方面,孔道有利于气体的扩散。也可以将铂碳粉末催化剂热压在PEM(质子交换膜)。通过如图3-2所示的制膜工艺,通过铂碳催化剂将2到5纳米铂颗粒负载到10纳米到80纳米的活性炭颗粒上,增加了铂的利用率。极片大小与氢气需求量正相关,即极片越大单位时间内同一电压/电流下制备的氢气量越多。In the cathode structure shown in Figure 3-1, the main active material of the cathode is platinum metal. The cathode structure can preferably be grid-like, as shown in Figure 3-1, platinum metal is plated on lead grid, titanium grid or alloy grid. On the one hand, this grid shape increases the electrochemical reaction area, which is conducive to the preparation of gas. ; On the other hand, the channel is conducive to the diffusion of gas. Platinum carbon powder catalyst can also be hot pressed on PEM (Proton Exchange Membrane). Through the film-making process shown in Figure 3-2, platinum particles of 2 to 5 nanometers are supported on activated carbon particles of 10 nanometers to 80 nanometers through a platinum-carbon catalyst, which increases the utilization rate of platinum. The size of the pole piece is positively correlated with the hydrogen demand, that is, the larger the pole piece is, the more hydrogen can be produced under the same voltage/current per unit time.

如图4-1所示的阳极的照片和图4-2所示的扫描电镜图,可明显看到图4-1中的网状结构,有利于电解水产生气体的排除,从而增加制氢效率。可明显看到微观结构上铅网表面的氧化铅片,可大大增加电解水面积,促进反应的进行。The photo of the anode shown in Figure 4-1 and the scanning electron microscope picture shown in Figure 4-2 show the network structure in Figure 4-1, which is conducive to the removal of gas generated by electrolysis of water, thereby increasing hydrogen production efficiency. The lead oxide flakes on the surface of the lead mesh on the microstructure can be clearly seen, which can greatly increase the area of electrolyzed water and promote the reaction.

通过图5所示阳极的水解性能曲线可知,采用对电极Ag/AgCl,电解液为0.5M 硫酸,电极面积1 cm2。图6为60℃下制氢装置性能曲线,电解液为0.5M 硫酸;阳极为铅网,电极面积1 cm2;阴极为铂片,电极面积0.7 cm2,可以看到8小时内,制氢装置运行稳定,几乎没有明显衰退。From the hydrolysis performance curve of the anode shown in Figure 5, it can be seen that the counter electrode Ag/AgCl is used, the electrolyte is 0.5M sulfuric acid, and the electrode area is 1 cm 2 . Figure 6 shows the performance curve of the hydrogen production device at 60°C. The electrolyte is 0.5M sulfuric acid; the anode is a lead grid with an electrode area of 1 cm 2 ; the cathode is a platinum sheet with an electrode area of 0.7 cm 2 . It can be seen that within 8 hours, hydrogen production The unit operated stably with little noticeable degradation.

本发明的基于铅网的水分解制氢装置的制备方法。The preparation method of the water splitting hydrogen production device based on the lead grid of the present invention.

步骤1,制备阳极铅网。采购铅箔,并用开孔机或者激光雕刻机在铅箔上开孔,制备成铅网;或者直接采购铅网;铅网可以直接用做阳极。Step 1, preparing the anode lead grid. Purchase lead foil, and use a punching machine or a laser engraving machine to open holes on the lead foil to prepare a lead grid; or directly purchase the lead grid; the lead grid can be directly used as an anode.

也可用溅射镀膜机在铅网上镀一层纳米铂金直接用作阳极。It is also possible to use a sputter coater to coat a layer of nano-platinum on the lead grid and directly use it as an anode.

也可把铅网放在装有浓氨水的聚四氟乙烯杯里,在180℃高温高压反应6小时到72小时,在铅网上生长一层氧化铅片用作阳极。The lead grid can also be placed in a polytetrafluoroethylene cup filled with concentrated ammonia water, and reacted under high temperature and high pressure at 180°C for 6 hours to 72 hours, and a layer of lead oxide sheet can be grown on the lead grid as an anode.

步骤2,制备阴极。用溅射镀膜机在铅箔上镀一层纳米铂金直接用作阴极。Step 2, preparing the cathode. A layer of nano-platinum gold was coated on the lead foil with a sputter coater and used as the cathode directly.

也可直接制作质子交换膜(PEM)燃料电池阳极用的铂碳PEM膜作为阴极和制氢装置的隔膜。Platinum carbon PEM membranes for proton exchange membrane (PEM) fuel cell anodes can also be directly fabricated as cathodes and diaphragms for hydrogen production devices.

步骤3,将质子交换膜隔置在阳极和阴极中间,并用外壳保护层和固定夹夹紧上述阳极-隔膜-阴极,即制备成了基于铅网的水分解制氢装置。In step 3, the proton exchange membrane is interposed between the anode and the cathode, and the above-mentioned anode-diaphragm-cathode is clamped with the shell protective layer and the fixing clip, that is, the water splitting hydrogen production device based on lead mesh is prepared.

基于铅网的水分解制氢装置的使用方法,其包括以下步骤。A method for using a water splitting hydrogen production device based on lead nets, comprising the following steps.

步骤1,将直流电源接口4与直流电源相连接,且阳极1与电源正极相连,阴极2与电源负极相连。Step 1, connect the DC power interface 4 to the DC power supply, and connect the anode 1 to the positive pole of the power supply, and connect the cathode 2 to the negative pole of the power supply.

步骤2,将基于铅网的水分解制氢装置置于酸性水溶液中,将直流电源接口4设置在液面上,且避免线路与水溶液相接触。Step 2, place the water splitting hydrogen production device based on the lead grid in the acidic aqueous solution, set the DC power interface 4 on the liquid surface, and avoid the contact between the circuit and the aqueous solution.

步骤3,打开电源开关,从2 V开始缓慢升高电压,根据氢气的需求量调整到合适的电压,如氢气需求量大则电压高,氢气需求量小则电压低。Step 3. Turn on the power switch, slowly increase the voltage from 2 V, and adjust to an appropriate voltage according to the hydrogen demand. If the hydrogen demand is large, the voltage will be high, and if the hydrogen demand is small, the voltage will be low.

步骤4,气体制备完成后,先把直流电源调整到低电压,然后关闭直流电源,最后断开直流电源接口4与直流电源的连接。Step 4, after the gas preparation is completed, first adjust the DC power supply to a low voltage, then turn off the DC power supply, and finally disconnect the DC power supply interface 4 from the DC power supply.

本发明的基于铅网的水分解制氢装置的设计,且装置能在高温下酸性中稳定运行而无明显衰退;本发明可应用于电催化水分解制氢体系;燃料电池体系;电催化制备氯气;有机小分子催化氧化。还需说明的是,图中各部件的形状和尺寸不反应真实大小和比例,而仅示意本发明实施例的内容。The design of the water splitting hydrogen production device based on the lead grid of the present invention, and the device can operate stably in acid at high temperature without obvious decline; the present invention can be applied to electrocatalytic water splitting hydrogen production system; fuel cell system; electrocatalytic preparation Chlorine gas; catalytic oxidation of small organic molecules. It should also be noted that the shapes and sizes of the components in the drawings do not reflect the actual sizes and proportions, but only illustrate the content of the embodiments of the present invention.

本发明未详细阐述部分属于本领域技术人员的公知技术。以上所述仅为本发明的较佳实施例,并不用以限制本发明,凡在本发明的精神和原则之内,所做的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Parts not described in detail in the present invention belong to the known techniques of those skilled in the art. The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included in the scope of the present invention. within the scope of protection.

Claims (7)

1.一种基于铅网的水分解制氢装置,其包括阳极、阴极和隔膜,其特征在于,其使用氧化铅薄片覆盖的铅网作为阳极,使用镀铂铅网或钛网或合金网作为阴极,使用质子交换膜(PEM)作为隔膜。1. A water splitting hydrogen production device based on a lead grid, which includes an anode, a cathode and a diaphragm, is characterized in that it uses a lead grid covered with lead oxide flakes as an anode, and uses a platinum-plated lead grid or a titanium grid or an alloy grid as an anode. For the cathode, a proton exchange membrane (PEM) is used as the separator. 2.根据权利要求1所述的基于铅网的水分解制氢装置,其特征在于:阳极、隔膜和阴极依序叠置构成水分解制氢装置主体。2. The water splitting hydrogen production device based on lead grid according to claim 1, characterized in that: the anode, the diaphragm and the cathode are sequentially stacked to form the main body of the water splitting hydrogen production device. 3.根据权利要求2所述的基于铅网的水分解制氢装置,其特征在于:在阳极的延伸段和阴极的延伸段分别设置有直流电源接口;在制氢过程中,直流电源通过直流电源接口与基于铅网的水分解制氢装置接通,电源负极中流出的电子通过阴极流入电解液,同时在阴极表面发生还原反应,阴极附近的电解液的氢离子得电子生成氢气。3. The water splitting hydrogen production device based on lead grid according to claim 2, characterized in that: the extension section of the anode and the extension section of the cathode are respectively provided with a DC power interface; The power supply interface is connected to the water splitting hydrogen production device based on the lead grid. The electrons flowing out of the negative electrode of the power supply flow into the electrolyte through the cathode, and at the same time, a reduction reaction occurs on the surface of the cathode. The hydrogen ions in the electrolyte near the cathode get electrons to generate hydrogen. 4.根据权利要求3所述的基于铅网的水分解制氢装置,其特征在于:质子交换膜(PEM)为全氟磺酸型质子交换膜、Nafion重铸膜、非氟聚合物质子交换膜或新型复合质子交换膜。4. The water splitting hydrogen production device based on lead grid according to claim 3, characterized in that: the proton exchange membrane (PEM) is perfluorosulfonic acid type proton exchange membrane, Nafion recast membrane, non-fluoropolymer proton exchange Membranes or new composite proton exchange membranes. 5.一种基于铅网的水分解制氢装置的制备方法,其特征在于,所述方法包括以下步骤:5. A preparation method of a lead net-based water splitting hydrogen production device, characterized in that the method comprises the following steps: 步骤1,制备阳极铅网;用溅射镀膜机在铅网上镀一层纳米铂金直接用作阳极;或者把铅网放在装有浓氨水的聚四氟乙烯杯里,在180℃高温高压反应6小时到72小时,在铅网上生长一层氧化铅片用作阳极;Step 1, prepare the anode lead grid; use a sputter coater to coat a layer of nano-platinum on the lead grid and use it directly as an anode; or put the lead grid in a polytetrafluoroethylene cup filled with concentrated ammonia water, and react under high temperature and high pressure at 180°C From 6 hours to 72 hours, grow a layer of lead oxide sheet on the lead grid as an anode; 步骤2,制备阴极,用溅射镀膜机在铅箔上镀一层纳米铂金直接用作阴极;Step 2, prepare the cathode, and use a sputter coater to coat a layer of nano-platinum gold on the lead foil directly as the cathode; 步骤3,将质子交换膜隔置在阳极和阴极中间,并用外壳保护层和固定夹夹紧上述阳极-隔膜-阴极,制备成了基于铅网的水分解制氢装置。In step 3, the proton exchange membrane is interposed between the anode and the cathode, and the above anode-diaphragm-cathode is clamped with the shell protective layer and the fixing clip, and a water splitting hydrogen production device based on lead mesh is prepared. 6.根据权利要求5所述的制备方法,其特征在于:6. The preparation method according to claim 5, characterized in that: 所述步骤2直接制作质子交换膜(PEM)燃料电池阳极用的铂碳PEM膜作为阴极和制氢装置的隔膜。The step 2 directly manufactures the platinum carbon PEM membrane for the anode of the proton exchange membrane (PEM) fuel cell as the cathode and the diaphragm of the hydrogen production device. 7.一种依据权利要求1-4之任一所述的基于铅网的水分解制氢装置的使用方法,其包括以下步骤:7. A method for using the lead grid-based water splitting hydrogen production device according to any one of claims 1-4, comprising the following steps: 步骤1,将直流电源接口与直流电源相连接,且阳极与直流电源正极相连,阴极与直流电源负极相连;Step 1, connect the DC power interface to the DC power supply, and connect the anode to the positive pole of the DC power supply, and connect the cathode to the negative pole of the DC power supply; 步骤2,将基于铅网的水分解制氢装置置于酸性水溶液中,将直流电源接口设置在液面上,且避免线路与水溶液相接触;Step 2, placing the water splitting hydrogen production device based on the lead grid in the acidic aqueous solution, setting the DC power interface on the liquid surface, and avoiding the contact between the circuit and the aqueous solution; 步骤3,打开电源开关,从2 V开始缓慢升高电压,根据氢气的需求量调整到合适的电压,如氢气需求量大则电压高,氢气需求量小则电压低;Step 3. Turn on the power switch, slowly increase the voltage from 2 V, and adjust to an appropriate voltage according to the hydrogen demand. If the hydrogen demand is large, the voltage will be high, and if the hydrogen demand is small, the voltage will be low; 步骤4,气体制备完成后,先把直流电源调整到低电压,然后关闭直流电源,最后断开直流电源接口与直流电源的连接。Step 4: After the gas preparation is completed, first adjust the DC power supply to a low voltage, then turn off the DC power supply, and finally disconnect the DC power supply interface from the DC power supply.
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US4456666A (en) * 1982-10-13 1984-06-26 Gnb Batteries Inc. Titanium wire reinforced lead composite electrode structure
CN87207164U (en) * 1987-06-10 1988-12-07 周昌明 Stereoscopic platinum anode electrolytic tank
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