CN113862690B - Water electrolysis hydrogen production device based on bipolar electrode system - Google Patents
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Abstract
Description
技术领域technical field
本发明属于水电解技术领域,特别是涉及一种基于双极电极体系电解水制氢装置。The invention belongs to the technical field of water electrolysis, in particular to a device for producing hydrogen by electrolyzing water based on a bipolar electrode system.
背景技术Background technique
能源是发展国民经济、提高人民生活质量的重要物质基础,是直接影响经济发展的重要制约因素,同时也是国家战略安全保障的基础之一。为解决经济发展与能源短缺及环境污染之间日益加剧的矛盾,开发清洁、高效、可持续发展的新能源动力技术已成为十分紧迫的任务。发展可再生能源和能源的清洁高效利用将是当今国际社会所面临的重要现实问题,对整个世界经济的可持续发展具有重要意义。氢能源作为高效、洁净和理想的二次能源已经受到了全世界的广泛重视。大规模、廉价地生产氢气是开发和利用氢能的重要环节之一。Energy is an important material basis for developing the national economy and improving people's quality of life, an important constraint that directly affects economic development, and one of the foundations for national strategic security. In order to solve the growing contradiction between economic development, energy shortage and environmental pollution, it has become a very urgent task to develop clean, efficient and sustainable new energy power technology. The development of renewable energy and the clean and efficient use of energy will be an important practical issue facing the international community today, and it is of great significance to the sustainable development of the entire world economy. As an efficient, clean and ideal secondary energy source, hydrogen energy has received extensive attention from all over the world. Large-scale and cheap production of hydrogen is one of the important links in the development and utilization of hydrogen energy.
如中国公开号CN105734600B公开一种三电极体系双电解槽两步法电解水制氢的装置及方法。该电解装置包含两个独立的电解槽(槽-1和槽-2)、析氢催化电极、析氧催化电极和氢氧化镍电极以及碱性电解质。该电解装置把电解水过程分为产氢和产氧两个步骤,并分别在两个电解槽(槽-1和槽-2)中交替进行;不能同时进行产氢和产氧,生产效率慢。For example, Chinese Publication No. CN105734600B discloses a device and method for producing hydrogen by electrolyzing water in a two-step method with a three-electrode system and double electrolyzers. The electrolysis device comprises two independent electrolytic cells (cell-1 and cell-2), a hydrogen evolution catalytic electrode, an oxygen evolution catalytic electrode, a nickel hydroxide electrode and an alkaline electrolyte. The electrolysis device divides the process of electrolyzing water into two steps of hydrogen production and oxygen production, which are carried out alternately in two electrolytic cells (cell-1 and cell-2); the production of hydrogen and oxygen cannot be performed at the same time, and the production efficiency is slow. .
发明内容Contents of the invention
本发明的目的在于提供一种基于双极电极体系电解水制氢装置,采用一块金属代替离子隔膜将电解槽中的碱液完全分隔,以泡沫镍及掺杂Co等材质为双极电极,通过两个电极端进行切换的活动电极的设置,同步分室完成产氢和产氧,降低隔离成本,提高生产效率和安全性。The purpose of the present invention is to provide a hydrogen production device based on bipolar electrode system electrolysis of water, which uses a piece of metal instead of an ion diaphragm to completely separate the lye in the electrolytic cell, and uses materials such as nickel foam and doped Co as bipolar electrodes. The setting of the active electrode for switching between the two electrode ends, synchronously separate chambers to complete hydrogen and oxygen production, reduce isolation costs, and improve production efficiency and safety.
为解决上述技术问题,本发明是通过以下技术方案实现的:In order to solve the problems of the technologies described above, the present invention is achieved through the following technical solutions:
本发明为一种基于双极电极体系电解水制氢装置,包括电解槽:电解槽内设置一金属材质的隔板并通过隔板分隔成独立的阳极析氧室和阴极析氢室;The present invention is a device for producing hydrogen by electrolyzing water based on a bipolar electrode system, including an electrolytic cell: a partition made of metal is arranged in the electrolytic cell and separated into an independent anode oxygen evolution chamber and a cathode hydrogen evolution chamber by the partition;
三个电极:对电解水生成氢气具有催化作用的析氢催化电极、对电解水生成氧气具有催化作用的析氧催化电极、以及双极电极;Three electrodes: a hydrogen evolution catalytic electrode that catalyzes the electrolysis of water to generate hydrogen, an oxygen evolution catalytic electrode that catalyzes the electrolysis of water to generate oxygen, and a bipolar electrode;
碱性电解液:在阳极析氧室中的产氧气,在阴极析氢室中的产氢气;所述双极电极为一可将位于所述阳极析氧室和阴极析氢室的两个电极端进行切换的活动电极;所述双极电极连接有控制双极电极两个电极端进行切换插入所述阳极析氧室和阴极析氢室的电极控制切换机构。Alkaline electrolyte: Oxygen is produced in the anode oxygen evolution chamber, and hydrogen is produced in the cathode hydrogen evolution chamber; The movable electrode for switching; the bipolar electrode is connected with an electrode control switching mechanism that controls the two electrode ends of the bipolar electrode to be switched and inserted into the anode oxygen evolution chamber and the cathode hydrogen evolution chamber.
进一步地,所述双极电极为一圆柱状结构;所述隔板上设置有与双极电极相配合的且呈竖直状设置的槽道;所述双极电极的顶部连接所述电极控制切换机构,所述电极控制切换机构为一包括电性连接的转动电机A和处理器;所述双极电极的材质为泡沫镍及掺杂钴,在碱液中镍表面发生阳极氧化生成Ni(OH)2/NiOOH氧化物覆盖层。Further, the bipolar electrode is a cylindrical structure; the separator is provided with a vertically arranged channel matching with the bipolar electrode; the top of the bipolar electrode is connected to the electrode control Switching mechanism, the electrode control switching mechanism is a rotating motor A and a processor that are electrically connected; the material of the bipolar electrode is nickel foam and doped cobalt, and anodic oxidation occurs on the nickel surface in the lye to generate Ni ( OH) 2 /NiOOH oxide capping layer.
进一步地,所述双极电极包括一U型电极本体,所述U型电极本体具有可分别插入阳极析氧室和阴极析氢室内的第一电极段和第二电极段;所述第一电极段和第二电极段均为泡沫镍,碱液中镍表面发生阳极氧化生成 Ni(OH)2/NiOOH氧化物覆盖层;所述U型电极本体的端部连接所述电极控制切换机构,所述电极控制切换机构包括一与U型电极本体连接的绝缘基板以及处理器,所述绝缘基板的上连接有电动伸缩机构,所述电动伸缩机构的端部连接有转动电机B;还包括设置所述阳极析氧室和阴极析氢室交汇处一侧的L型支架,所述转动电机B安装在所述L型支架上;且所述处理器分别连接电动伸缩机构和转动电机B。Further, the bipolar electrode includes a U-shaped electrode body, and the U-shaped electrode body has a first electrode segment and a second electrode segment that can be respectively inserted into the anode oxygen evolution chamber and the cathode hydrogen evolution chamber; the first electrode segment and the second electrode segment are foamed nickel, and anodic oxidation occurs on the nickel surface in the lye to generate Ni(OH)2/NiOOH oxide covering layer; the end of the U-shaped electrode body is connected to the electrode control switching mechanism, and the The electrode control switching mechanism includes an insulating substrate connected to the U-shaped electrode body and a processor, an electric telescopic mechanism is connected on the insulating substrate, and a rotating motor B is connected to the end of the electric telescopic mechanism; it also includes setting the The L-shaped bracket on the side where the anode oxygen evolution chamber and the cathode hydrogen evolution chamber meet, the rotating motor B is installed on the L-shaped bracket; and the processor is connected to the electric telescopic mechanism and the rotating motor B respectively.
所述析氢催化电极的电极材料为:基于金属铂以及其与碳的复合物;或基于Ni、Co或Fe过渡金属的单质或化合物;或基于Cu的化合物;或基于W的化合物;基于Mo的化合物;所述析氧催化电极的电极材料为:基于 Ru或Ir贵金属的化合物;或基于Ni、Co、Fe或Mn过渡金属的单质或化合物;所述碱性电解质溶液选自氢氧化钾、氢氧化钠以及其他碱性水溶液。The electrode material of the hydrogen evolution catalytic electrode is: based on metal platinum and its compound with carbon; or based on the simple substance or compound of Ni, Co or Fe transition metal; or based on Cu compound; or based on W compound; based on Mo compound; the electrode material of the oxygen evolution catalytic electrode is: a compound based on Ru or Ir noble metal; or a simple substance or compound based on Ni, Co, Fe or Mn transition metal; the alkaline electrolyte solution is selected from potassium hydroxide, hydrogen Sodium oxide and other alkaline aqueous solutions.
进一步地,所述阳极析氧室和阴极析氢室上分别设置有氧气收集器和氢气收集器的出口;所述氧气收集器和/或氢气收集器处连接有用于检测气体流量的流量传感器,所述流量传感器与所述处理器连接。Further, the anode oxygen evolution chamber and the cathode hydrogen evolution chamber are respectively provided with outlets of an oxygen collector and a hydrogen collector; the oxygen collector and/or the hydrogen collector are connected with a flow sensor for detecting gas flow, so The flow sensor is connected to the processor.
所述阳极析氧室和阴极析氢室的底部均设置有一进碱液口,所述进碱液口连通有进液系统,所述进液系统包括一与所述进碱液口连通的进液泵,所述进液泵设置在所述碱液槽内。The bottoms of the anode oxygen evolution chamber and the cathode hydrogen evolution chamber are provided with a lye inlet, and the lye inlet is connected with a liquid inlet system, and the liquid inlet system includes a liquid inlet communicated with the lye inlet. A pump, the liquid inlet pump is arranged in the lye tank.
本发明具有以下有益效果:The present invention has the following beneficial effects:
本发明通过两个电极端进行切换的活动电极的设置,通过在电解过程智能的进行电极端的切换,从而完成在一个装置系统内同时不同空间完成产氢和产氧,提高整体的生产效率。In the present invention, through the setting of movable electrodes for switching between two electrode ends, the electrode ends are switched intelligently during the electrolysis process, so as to complete hydrogen production and oxygen production in different spaces at the same time in one device system, and improve the overall production efficiency.
当然,实施本发明的任一产品并不一定需要同时达到以上所述的所有优点。Of course, any product implementing the present invention does not necessarily need to achieve all the above-mentioned advantages at the same time.
附图说明Description of drawings
为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述所需要使用的附图作简单地介绍,显而易见地,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following will briefly introduce the accompanying drawings that are required for the description of the embodiments. Obviously, the accompanying drawings in the following description are only some embodiments of the present invention. Those of ordinary skill in the art can also obtain other drawings based on these drawings without any creative effort.
图1为本发明电解水制氢装置结构示意图一;Fig. 1 is a schematic diagram of the structure of the electrolyzed water hydrogen production device of the present invention;
图2为本发明电解水制氢装置结构示意图二;Fig. 2 is a structural schematic diagram II of the electrolyzed water hydrogen production device of the present invention;
图3为本发明氢氧化镍电极结构示意图。Fig. 3 is a schematic diagram of the structure of the nickel hydroxide electrode of the present invention.
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作出创造性劳动前提下所获得的所有其它实施例,都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 accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some, not all, embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.
在本发明的描述中,需要理解的是,术语“开孔”、“上”、“下”、“厚度”、“顶”、“中”、“长度”、“内”、“四周”等指示方位或位置关系,仅是为了便于描述本发明和简化描述,而不是指示或暗示所指的组件或元件必须具有特定的方位,以特定的方位构造和操作,因此不能理解为对本发明的限制。In describing the present invention, it is to be understood that the terms "opening", "upper", "lower", "thickness", "top", "middle", "length", "inner", "surrounding" etc. Indicating orientation or positional relationship is only for the convenience of describing the present invention and simplifying the description, and does not indicate or imply that the components or elements referred to must have a specific orientation, be constructed and operated in a specific orientation, and therefore cannot be construed as limiting the present invention .
请参阅图1-2所示,本发明为一种基于双极电极体系电解水制氢装置,包括一个电解槽,通过一块金属分割成独立的阳极析氧室1和阴极析氢室2;三个电极:对电解水生成氢气具有催化作用的析氢催化电极21、对电解水生成氧气具有催化作用的析氧催化电极11、以及泡沫镍及掺杂Co等材质为双极电极,3;碱性电解液:在阳极析氧室1中的产氧气,在阴极析氢室2 中的产氢气;泡沫镍以及掺杂钴等双极电极3为一可将位于阳极析氧室1 和阴极析氢室2的两个电极端进行切换的活动电极;双极电极3连接有控制双极电极3两个电极端进行切换插入阳极析氧室1和阴极析氢室2的电极控制切换机构;析氢催化电极21的材质为Co2O3,析氧催化电极11的材质为RuO2。Please refer to Fig. 1-2, the present invention is a water electrolysis hydrogen production device based on a bipolar electrode system, including an electrolytic cell, which is divided into independent anode oxygen evolution chamber 1 and cathode
且析氢催化电极21和析氧催化电极11分别连接电源正负极。And the hydrogen evolution
在阴极析氢室2中:In cathode hydrogen evolution chamber 2:
水分子在作为阴极的析氢催化电极21表面被电化学还原成氢气,即H2O +e-→1/2H2+OH-;同时作为阳极的Ni(OH)2电极被电化学氧化为NiOOH 电极,即Ni(OH)2+OH--e-→NiOOH+H2O,当阴极析氢室2中Ni(OH)2几乎全被氧化成NiOOH,阴极析氢室2中形成的NiOOH电极被转移至阳极析氧室1,用于电解水产氧;Water molecules are electrochemically reduced to hydrogen on the surface of the hydrogen evolution
在阳极析氧室1中:In the anode oxygen evolution chamber 1:
作为阴极的NiOOH电极被电化学还原成为Ni(OH)2电极,即NiOOH+H2O +e-→Ni(OH)2+OH-;同时氢氧根离子在作为阳极的析氧催化电极11表面被电化学氧化成为氧气,即2OH--2e-→1/2O2+H2O;当阳极析氧室1 中NiOOH被还原成Ni(OH)2,阳极析氧室1中形成的Ni(OH)2电极被转移至阴极析氢室2,并再用于电解水产氢;The NiOOH electrode as the cathode is electrochemically reduced to become the Ni(OH) 2 electrode, that is, NiOOH+H 2 O +e-→Ni(OH) 2 +OH - The surface is electrochemically oxidized to oxygen, that is, 2OH - -2e-→1/2O 2 +H 2 O; when NiOOH in the anode oxygen evolution chamber 1 is reduced to Ni(OH) 2 , the Ni formed in the anode oxygen evolution chamber 1 The (OH) 2 electrode is transferred to the cathode
实施例2,基于实施例1的;
如图2和3,阳极析氧室1和阴极析氢室2之间连通有一隔板4,双极电极3为一圆柱状结构;隔板4上设置有与双极电极3相配合的且呈竖直状设置的槽道41;双极电极3的顶部连接电极控制切换机构,电极控制切换机构为一包括电性连接的转动电机A和处理器。As shown in Figures 2 and 3, a
双极电极3包括位于中间的绝缘隔板31,绝缘隔板31的两侧分别设置有截面呈半圆形的电极棒32,两个电极棒32均为泡沫镍及掺杂Co等材质;绝缘隔板31的顶部设置有与转动电机A相连接的安装板33;两电极棒32 的顶部电性连接;位于安装板33正下方的绝缘隔板31上设置有贯穿绝缘隔板31的导电结构34、且导电结构34的两端分别连接两电极棒32的导电结构34,导电结构34为泡沫镍及掺杂Co等材质;绝缘隔板31的两侧分别设置有一对可与槽道41呈密封配合的密封翻边35,位于绝缘隔板31同一侧的两密封翻边35对称设置,密封翻边35呈弧形。The
使用时,通过柱状的双极电极3的设置,实现在进行电解水过程中可根据需求任意时刻调整双极电极3转动将双极电极3的两个电极端切换性的放入阳极析氧室1和阴极析氢室2,从而循环的进行氧化和还原反应。When in use, through the setting of the columnar
实施例3,基于实施例1的;
如图1、Ni(OH)2/NiOOH双极电极3包括一U型电极本体301,U型电极本体301具有可分别插入阳极析氧室1和阴极析氢室2内的第一电极段302 和第二电极段303,第一电极段302和第二电极段303均为泡沫镍及掺杂 Co等材质;U型电极本体301的端部连接电极控制切换机构,电极控制切换机构包括一与U型电极本体301连接的绝缘基板5以及处理器,绝缘基板5的上连接有电动伸缩机构51,电动伸缩机构51的端部连接有转动电机 B53;还包括设置阳极析氧室1和阴极析氢室2交汇处一侧的L型支架54,转动电机B53安装在L型支架54上;且处理器分别连接电动伸缩机构51 和转动电机B53。As shown in Fig. 1, Ni(OH) 2 /NiOOH
实施例4,基于实施例1-3的;
如图1和2,阳极析氧室1和阴极析氢室2上分别有氧气收集器和氢气收集器的出口;氧气收集器和/或氢气收集器处连接有用于检测气体流量的流量传感器,流量传感器与处理器连接。通过流量传感器检测气体的流量判断电解速度,从而判断位于是阳极析氧室1和阴极析氢室2内的双极电极3的表面氧化还原程度,方便及时的将双极电极3的两个电极端切换性的放入阳极析氧室1和阴极析氢室2内,避免因双极电极3的自身状况影响电解速度。As shown in Figures 1 and 2, the anode oxygen evolution chamber 1 and the cathode
实施例5、基于实施例1-3的;
阳极析氧室1和阴极析氢室2的底部均设置有一进碱液口7,进碱液口 7连通有进液系统,进液系统包括一与进碱液口7连通的进液泵,进液泵设置在碱液槽内。The bottoms of the anode oxygen evolution chamber 1 and the cathode
在本说明书的描述中,参考术语“一个实施例”、“示例”、“具体示例”等的描述意指结合该实施例或示例描述的具体特征、结构、材料或者特点包含于本发明的至少一个实施例或示例中。在本说明书中,对上述术语的示意性表述不一定指的是相同的实施例或示例。而且,描述的具体特征、结构、材料或者特点可以在任何的一个或多个实施例或示例中以合适的方式结合。In the description of this specification, descriptions with reference to the terms "one embodiment", "example", "specific example" and the like mean that the specific features, structures, materials or characteristics described in conjunction with the embodiment or example are included in at least one embodiment of the present invention. In an embodiment or example. In this specification, schematic representations of the above terms do not necessarily refer to the same embodiment or example. Furthermore, the specific features, structures, materials or characteristics described may be combined in any suitable manner in any one or more embodiments or examples.
以上公开的本发明优选实施例只是用于帮助阐述本发明。优选实施例并没有详尽叙述所有的细节,也不限制该发明仅为所述的具体实施方式。显然,根据本说明书的内容,可作很多的修改和变化。本说明书选取并具体描述这些实施例,是为了更好地解释本发明的原理和实际应用,从而使所属技术领域技术人员能很好地理解和利用本发明。本发明仅受权利要求书及其全部范围和等效物的限制。The preferred embodiments of the invention disclosed above are only to help illustrate the invention. The preferred embodiments are not exhaustive in all detail, nor are the inventions limited to specific embodiments described. Obviously, many modifications and variations can be made based on the contents of this specification. This description selects and specifically describes these embodiments in order to better explain the principle and practical application of the present invention, so that those skilled in the art can well understand and utilize the present invention. The invention is to be limited only by the claims, along with their full scope and equivalents.
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