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CN114934291B - A partitioned electrode of an alkaline water electrolyzer based on non-uniform electrodeposition and its preparation method - Google Patents

A partitioned electrode of an alkaline water electrolyzer based on non-uniform electrodeposition and its preparation method Download PDF

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CN114934291B
CN114934291B CN202210473733.1A CN202210473733A CN114934291B CN 114934291 B CN114934291 B CN 114934291B CN 202210473733 A CN202210473733 A CN 202210473733A CN 114934291 B CN114934291 B CN 114934291B
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electrodeposition
alkaline water
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CN114934291A (en
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张存满
金黎明
吕洪
耿振
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Tongji University
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Abstract

本发明涉及一种基于非均匀电沉积的碱水电解槽分区电极及制备方法,所述电极包括电极基体和用于给电极基体提供电流输入的电极接线柱;所述电极基体的两端分别对应电解槽的进口测和出口测,所述电极基体表面沉积有催化剂层,所述催化剂层中的催化剂密度沿着电解槽的进口测至出口测方向梯度降低。与现有技术相比,本发明具有产氢效率高的优点。

The invention relates to a partitioned electrode of an alkaline water electrolytic cell based on non-uniform electrodeposition and a preparation method thereof. The electrode includes an electrode base and an electrode terminal for providing current input to the electrode base; the two ends of the electrode base correspond to The inlet side and the outlet side of the electrolytic cell, a catalyst layer is deposited on the surface of the electrode substrate, and the catalyst density in the catalyst layer decreases along the gradient from the inlet side to the outlet side of the electrolytic cell. Compared with the prior art, the invention has the advantage of high hydrogen production efficiency.

Description

一种基于非均匀电沉积的碱水电解槽分区电极及制备方法A kind of partition electrode of alkaline water electrolyzer based on non-uniform electrodeposition and preparation method

技术领域technical field

本发明涉及碱水电解制氢技术领域,尤其是涉及一种基于非均匀电沉积的碱水电解槽分区电极及制备方法。The invention relates to the technical field of hydrogen production by alkaline water electrolysis, in particular to a partitioned electrode of an alkaline water electrolyzer based on non-uniform electrodeposition and a preparation method thereof.

背景技术Background technique

电解水制氢是目前最常用的制氢技术之一,其中碱水电解制氢技术相对成熟,已经实现了商业化,随着市场需求的增加,碱水电解槽的尺寸和产能不断增大,未来单台套的电解槽直径将超过2m,产能超过1500Nm3/h。电极是电解槽的核心部件,尺寸和产能的增加对电极提出了更高的要求,需要在现有镍网电极的基础上,增大电极面积,负载高性能催化剂等。Hydrogen production by electrolysis of water is one of the most commonly used hydrogen production technologies at present. Among them, the hydrogen production technology by electrolysis of alkaline water is relatively mature and has been commercialized. With the increase of market demand, the size and production capacity of alkaline water electrolysis cells continue to increase. In the future, the diameter of a single set of electrolytic cell will exceed 2m, and the production capacity will exceed 1500Nm3/h. The electrode is the core component of the electrolyzer. The increase in size and capacity puts forward higher requirements on the electrode. It is necessary to increase the electrode area and load high-performance catalysts on the basis of the existing nickel mesh electrode.

电解槽的大型化必然会导致电解槽径向温度分布不均匀,靠近碱液进口测温度较低,靠近出口测温度较高。进口测方向温度低,反应活性低,产氢效率低,而出口测方向温度高使得产氢速率过快导致气阻。因此不同位置对电极反应过程的需求也不同。The enlargement of the electrolytic cell will inevitably lead to uneven temperature distribution in the radial direction of the electrolytic cell. The temperature measured near the lye inlet is lower and the temperature near the outlet is higher. The inlet temperature is low, the reaction activity is low, and the hydrogen production efficiency is low, while the outlet temperature is high, so the hydrogen production rate is too fast, resulting in air resistance. Therefore, different positions have different requirements for the electrode reaction process.

针对上述问题,结合电解液内部的反应特点,亟需对于大面积电解槽使用的电极在径向分布进行设计,以迎合大型电解槽不同位置的反应需求,从而提升电解槽的产氢效率。In view of the above problems, combined with the reaction characteristics inside the electrolyte, it is urgent to design the radial distribution of electrodes used in large-area electrolyzers to meet the reaction needs of different positions in large-scale electrolyzers, thereby improving the hydrogen production efficiency of electrolyzers.

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了一种产氢效率高的基于非均匀电沉积的碱水电解槽分区电极及制备方法,以迎合大型电解槽电极不同位置的反应需求。The purpose of the present invention is to overcome the above-mentioned defects in the prior art and provide a highly efficient hydrogen production based on non-uniform electrodeposition alkaline water electrolyzer partition electrode and preparation method to cater to the reaction of different positions of large electrolyzer electrodes need.

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:

根据本发明的第一方面,提供了一种基于非均匀电沉积的碱水电解槽分区电极,包括电极基体和用于给电极基体提供电流输入的电极接线柱;所述电极基体的两端分别对应电解槽的进口测和出口测,所述电极基体表面沉积有催化剂层,所述催化剂层中的催化剂密度沿着电解槽的进口测至出口测方向梯度降低。According to the first aspect of the present invention, a kind of alkaline water electrolyzer partition electrode based on non-uniform electrodeposition is provided, comprising an electrode base and an electrode terminal for providing current input to the electrode base; the two ends of the electrode base are respectively Corresponding to the inlet side and outlet side of the electrolytic cell, a catalyst layer is deposited on the surface of the electrode substrate, and the catalyst density in the catalyst layer decreases gradually along the direction from the inlet side to the outlet side of the electrolytic cell.

优选地,所述电极基体为金属编织网基体,其材质包括镍基、铁基或合金。Preferably, the electrode substrate is a metal braided mesh substrate, and its material includes nickel base, iron base or alloy.

优选地,所述电极基体的形状包括圆形和方形。Preferably, the shapes of the electrode base include circle and square.

优选地,所述电极基体上的催化剂密度等梯度降低。Preferably, the density of the catalyst on the electrode base decreases isogradiently.

优选地,所述电极接线柱的数量至少为1。Preferably, the number of the electrode terminals is at least one.

根据本发明的第二方面,提供了一种用于上述基于非均匀电沉积的碱水电解槽分区电极的制备方法,该方法包括:将电极基体垂重悬挂,利用电极接线柱向电极基体输入电流,将电极基体分N次逐步浸入电解液,进行电沉积,结束后得到梯度分布电极。According to the second aspect of the present invention, there is provided a preparation method for the partition electrode of the above-mentioned alkaline water electrolyzer based on non-uniform electrodeposition. Current, the electrode substrate is gradually immersed in the electrolyte for N times, and electrodeposition is carried out, and a gradient distribution electrode is obtained after the end.

优选地,所述N为1~50。Preferably, the N is 1-50.

优选地,所述N为3-20。Preferably, the N is 3-20.

优选地,每一步的电沉积时间范围为1min~24h。Preferably, the electrodeposition time of each step ranges from 1 min to 24 h.

优选地,每一步的电沉积时间范围为5min~2h。Preferably, the electrodeposition time of each step ranges from 5 minutes to 2 hours.

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:

本发明通过电极结构设计和梯度分布催化剂电极制备,进口测催化剂密度高,一方面能够增加欧姆电阻提升进口处产热,提升电解液温度,另一方面增加催化剂密度能够增加反应活性位点,提升产氢效率;随着电解液温度升高降低催化剂密度,避免出现产氢速率过快导致气阻;出口测催化剂密度较低能够显著降低产氢效率和产热,避免气阻发生,有效提升电解槽的综合产氢效率提升电极的综合产氢效率,符合电解槽进出口温度特性及电极反应需求,能够从本质上提升电极产氢效率。The invention adopts electrode structure design and gradient distribution catalyst electrode preparation, and the inlet test catalyst density is high. On the one hand, the ohmic resistance can be increased to increase the heat production at the inlet, and the temperature of the electrolyte can be increased. On the other hand, increasing the catalyst density can increase the reaction active sites and improve Hydrogen production efficiency; as the temperature of the electrolyte increases, the catalyst density is reduced to avoid air lock caused by too fast a hydrogen production rate; the lower catalyst density at the outlet can significantly reduce the hydrogen production efficiency and heat production, avoid the occurrence of air lock, and effectively improve electrolysis The comprehensive hydrogen production efficiency of the cell improves the comprehensive hydrogen production efficiency of the electrode, which meets the temperature characteristics of the inlet and outlet of the electrolytic cell and the electrode reaction requirements, and can essentially improve the hydrogen production efficiency of the electrode.

附图说明Description of drawings

图1为本发明的基于非均匀电沉积的碱水电解槽分区电极示意图;Fig. 1 is the partition electrode schematic diagram of alkaline water electrolyzer based on heterogeneous electrodeposition of the present invention;

图2为实施例2中的电极电沉积过程示意图;其中,图2a为X1时间电沉积电极结构示意图;图2b为X1+X2时间电沉积电极结构示意图;图2c为X1+X2+X3时间电沉积电极结构示意图;图2d为X1+X2+X3+X4时间电沉积电极结构示意图;Fig. 2 is the schematic diagram of electrodeposition process in embodiment 2; Wherein, Fig. 2 a is the schematic diagram of X1 time electrodeposition electrode structure; Fig. 2 b is X1+X2 time electrodeposition electrode structure schematic diagram; Fig. 2 c is X1+X2+X3 time electrodeposition diagram Schematic diagram of the electrodeposition structure; Figure 2d is a schematic diagram of the electrodeposition electrode structure at X1+X2+X3+X4 time;

其中,1-电极基体,2-电极接线柱。Among them, 1-electrode substrate, 2-electrode terminal.

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,所描述的实施例是本发明的一部分实施例,而不是全部实施例。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的前提下所获得的所有其他实施例,都应属于本发明保护的范围。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. Obviously, the described embodiments are part 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 shall fall within the protection scope of the present invention.

实施例1Example 1

本实施例给出了一种基于非均匀电沉积的碱水电解槽分区电极,包括电极基体1和用于给电极基体1提供电流输入的电极接线柱2;所述电极基体1的两端分别对应电解槽的进口测和出口测,所述电极基体1表面沉积有催化剂层,所述催化剂层中的催化剂密度沿着电解槽的进口测至出口测方向梯度降低。This embodiment provides a partition electrode for alkaline water electrolyzer based on non-uniform electrodeposition, including an electrode base 1 and an electrode terminal 2 for providing current input to the electrode base 1; the two ends of the electrode base 1 are respectively Corresponding to the inlet side and outlet side of the electrolytic cell, a catalyst layer is deposited on the surface of the electrode substrate 1, and the catalyst density in the catalyst layer decreases gradually along the direction from the inlet side to the outlet side of the electrolytic cell.

所述电极基体1为金属编织网基体,可以为均匀分布的金属丝基体也可延伸为非均匀结构。其材质可以为镍基、铁基及其它不同金属或金属合金材料。The electrode base 1 is a metal braided mesh base, which can be a uniformly distributed metal wire base or extend into a non-uniform structure. Its material can be nickel base, iron base and other different metals or metal alloy materials.

所述电极基体1的形状包括圆形和方形以及其他任何几何形状。The shape of the electrode base 1 includes circle, square and any other geometric shapes.

所述电极接线柱2的数量至少为1。The number of the electrode terminals 2 is at least one.

接下来给出本发明的方法实施例,一种用于上述基于非均匀电沉积的碱水电解槽分区电极的制备方法,该方法包括:将电极基体1垂重悬挂,利用电极接线柱2向电极基体1输入电流,将电极基体1分N次逐步浸入电解液,进行电沉积,结束后得到梯度分布电极。其中,电极下端的电沉积时间长,催化剂密度高,依次往上逐级递减。Next, a method embodiment of the present invention is given, a preparation method for the above-mentioned partitioned electrode of an alkaline water electrolyzer based on non-uniform electrodeposition, the method includes: hanging the electrode base 1 vertically, using the electrode terminal The electrode base 1 is input with current, and the electrode base is gradually immersed in the electrolyte for N times in one minute, for electrodeposition, and a gradient distribution electrode is obtained after the end. Among them, the electrodeposition time at the lower end of the electrode is long, and the catalyst density is high, which gradually decreases step by step upward.

其中,N为1~50,尤其是3-20;每一步的电沉积时间范围为1min~24h,尤其是5min~2h。Wherein, N is 1-50, especially 3-20; the electrodeposition time range of each step is 1min-24h, especially 5min-2h.

实施例2Example 2

以镍金属丝均匀编织的镍网为电极基体1,在电极基体1表面沉积催化剂,电流通过电极接线柱2从电极基体1顶端输入,其中,电极接线柱2数量为1。将电极基体的1/4浸入含镍、铁的电解液中,通过电沉积在镍网表面沉积镍铁合金,沉积时间为20min-2h;沉积结束后,将电极基体进一步往下,直至电极基体的1/2浸入含镍、铁的电解液中,通过电沉积在镍网表面沉积镍铁合金,沉积时间为20min-2h;沉积结束后,将电极基体进一步往下,直至电极基体的3/4浸入含镍、铁的电解液中,通过电沉积在镍网表面沉积镍铁合金,沉积时间为20min-2h;沉积结束后,将电极基体进一步往下,直至电极基体全部浸入含镍、铁的电解液中,通过电沉积在镍网表面沉积镍铁合金,沉积时间为20min-2h,最终获得梯度分布的电极。The nickel mesh uniformly woven with nickel metal wires is used as the electrode base 1, and the catalyst is deposited on the surface of the electrode base 1, and the current is input from the top of the electrode base 1 through the electrode terminal 2, wherein the number of the electrode terminal 2 is 1. Immerse 1/4 of the electrode base in the electrolyte containing nickel and iron, and deposit nickel-iron alloy on the surface of the nickel mesh by electrodeposition. The deposition time is 20min-2h; 1/2 is immersed in the electrolyte containing nickel and iron, and the nickel-iron alloy is deposited on the surface of the nickel mesh by electrodeposition. The deposition time is 20min-2h; after the deposition is completed, the electrode substrate is further down until 3/4 of the electrode substrate is immersed In the electrolyte containing nickel and iron, the nickel-iron alloy is deposited on the surface of the nickel mesh by electrodeposition, and the deposition time is 20min-2h; after the deposition is completed, the electrode substrate is further lowered until the electrode substrate is completely immersed in the electrolyte containing nickel and iron In the process, the nickel-iron alloy is deposited on the surface of the nickel mesh by electrodeposition, and the deposition time is 20min-2h, and the electrodes with gradient distribution are finally obtained.

以上所述,仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到各种等效的修改或替换,这些修改或替换都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应以权利要求的保护范围为准。The above is only a specific embodiment of the present invention, but the protection scope of the present invention is not limited thereto. Any person familiar with the technical field can easily think of various equivalents within the technical scope disclosed in the present invention. Modifications or replacements shall all fall within the protection scope of the present invention. Therefore, the protection scope of the present invention should be based on the protection scope of the claims.

Claims (10)

1. An alkaline water electrolysis cell partition electrode based on non-uniform electrodeposition, which is characterized by comprising an electrode substrate (1) and an electrode binding post (2) for providing current input to the electrode substrate (1); the two ends of the electrode matrix (1) respectively correspond to the inlet side and the outlet side of the electrolytic tank, a catalyst layer is deposited on the surface of the electrode matrix (1), and the catalyst density in the catalyst layer is reduced in a gradient manner along the direction from the inlet side to the outlet side of the electrolytic tank.
2. The alkaline water electrolysis cell partition electrode based on non-uniform electrodeposition according to claim 1, wherein the electrode substrate (1) is a metal woven mesh substrate, and the material of the electrode substrate comprises nickel base, iron base or alloy.
3. The alkaline water cell partition electrode based on non-uniform electrodeposition according to claim 1, wherein the shape of the electrode base (1) comprises a circular shape and a square shape.
4. The alkaline water cell partition electrode based on non-uniform electrodeposition according to claim 1, wherein the catalyst density on the electrode substrate (1) is reduced with an equal gradient.
5. The alkaline water cell partition electrode based on non-uniform electrodeposition according to claim 1, wherein the number of electrode studs (2) is at least 1.
6. A method for preparing a partitioned electrode for a non-uniform electrodeposition-based alkaline water electrolysis cell according to claim 1, comprising: and (3) hanging the electrode matrix (1) vertically, inputting current to the electrode matrix (1) by using the electrode binding post (2), immersing the electrode matrix (1) into electrolyte step by step for N times, and carrying out electrodeposition to obtain the gradient distribution electrode after the completion of electrodeposition.
7. The method of claim 6, wherein N is 1 to 50.
8. The method of claim 7, wherein N is 3-20.
9. The method of claim 6, wherein the electrodeposition time of each step is in the range of 1min to 24h.
10. The method of claim 9, wherein the electrodeposition time of each step is in the range of 5min to 2h.
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