WO2023093012A1 - Method for triple-electrode system electrolyzing water to produce hydrogen - Google Patents

Method for triple-electrode system electrolyzing water to produce hydrogen Download PDF

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WO2023093012A1
WO2023093012A1 PCT/CN2022/099672 CN2022099672W WO2023093012A1 WO 2023093012 A1 WO2023093012 A1 WO 2023093012A1 CN 2022099672 W CN2022099672 W CN 2022099672W WO 2023093012 A1 WO2023093012 A1 WO 2023093012A1
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electrode
plate
circuit
hydrogen
frame
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PCT/CN2022/099672
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French (fr)
Chinese (zh)
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王凡
王金意
余智勇
刘丽萍
王韬
郭海礁
王鹏杰
任志博
张畅
徐显明
潘龙
Original Assignee
中国华能集团清洁能源技术研究院有限公司
四川华能氢能科技有限公司
华能集团技术创新中心有限公司
四川华能太平驿水电有限责任公司
四川华能宝兴河水电有限责任公司
四川华能嘉陵江水电有限责任公司
四川华能东西关水电股份有限公司
四川华能康定水电有限责任公司
四川华能涪江水电有限责任公司
华能明台电力有限责任公司
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Publication of WO2023093012A1 publication Critical patent/WO2023093012A1/en

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    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/01Products
    • C25B1/02Hydrogen or oxygen
    • C25B1/04Hydrogen or oxygen by electrolysis of water
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B1/00Electrolytic production of inorganic compounds or non-metals
    • C25B1/50Processes
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25BELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
    • C25B9/00Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
    • C25B9/17Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
    • 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

Definitions

  • the present application relates to the technical field of hydrogen production by electrolysis of water, in particular to a method for hydrogen production by electrolysis of water with a three-electrode system.
  • the existing electrolyzer is a combination of many electrolytic chambers, and the main components of each electrolytic chamber are cathode, anode, diaphragm and electrolyte.
  • Conventional water electrolysis technology generates hydrogen and oxygen at the cathode and anode during the electrode process, which will easily lead to the mixing of hydrogen and oxygen, making the prepared gas impure, and the subsequent purification will greatly increase the production cost.
  • Using an ion-selective membrane to separate the hydrogen generated at the hydrogen evolution catalytic electrode and the oxygen generated at the oxygen evolution catalytic electrode is an effective solution, but the use of the ion-selective membrane also greatly increases the cost.
  • the rates of hydrogen and oxygen production are different.
  • the pressure on both sides of the ion-selective membrane is different, the loss of the membrane is also very serious, which further increases the cost.
  • the selective ion exchange membrane further increases the internal resistance of the electrolyzer and increases energy consumption.
  • the current mainstream work is to improve or prepare a new type of diaphragm, in order to reduce the internal resistance while taking into account the hydrophilicity, ion permeability and the ability to completely separate hydrogen and oxygen. Although many new diaphragms have been researched and explored, the effect is still not very significant.
  • This application aims to solve one of the technical problems in the related art at least to a certain extent.
  • the purpose of this application is to propose a method for producing hydrogen by electrolyzing water with a three-electrode system.
  • the two circuits realize the separate preparation of hydrogen and oxygen by controlling the closing and opening of the two circuits, so that the prepared hydrogen and oxygen will not mix, simplify the separation cost, and the control method is simple and easy to operate.
  • a method for producing hydrogen by electrolyzing water with a three-electrode system includes:
  • a first circuit is formed between the hydrogen evolution cathode plate, the auxiliary electrode plate and the external power supply in the electrolytic cell, and a second circuit is formed between the auxiliary electrode plate, the oxygen evolution anode plate and the external power supply, so as to be closed by the first circuit and the second circuit is disconnected so that a reaction occurs on the hydrogen evolution cathode plate: H 2 O+e - ⁇ 1/2H 2 +OH - , hydrogen gas is prepared, and the first circuit is disconnected and the second Closing the circuit causes a reaction to occur on the oxygen evolution anode plate: OH - -e - ⁇ 1/4O 2 +1/2H 2 O, and oxygen is produced.
  • a retaining ring is sealed between the cathode electrode frame and the auxiliary electrode frame and between the auxiliary electrode frame and the anode electrode frame to obtain a three-electrode assembly.
  • it also includes stacking a plurality of three-electrode assemblies sequentially in the order of the cathode electrode frame, the auxiliary electrode frame, and the anode electrode frame to form a three-electrode system.
  • the electrolysis cavity enclosed between the cathode electrode frame, the auxiliary electrode frame and the retaining ring, the auxiliary electrode frame, and the anode in each three-electrode assembly in the three-electrode system through the liquid flow holes on the end pressure plate and the insulating plate.
  • Potassium hydroxide electrolyte is passed into the electrolytic cavity enclosed between the electrode frame and the guard ring.
  • the hydrogen evolution cathode plate is one of nickel-based alloy hydrogen evolution electrode, porous nickel hydrogen evolution electrode, nickel-based noble metal oxide hydrogen evolution electrode and nickel-based dispersion composite hydrogen evolution electrode.
  • oxygen evolution anode plate is an alloy electrode with nickel, cobalt, and iron as effective catalytic components.
  • the auxiliary electrode plate is a nickel hydroxide electrode.
  • a reaction occurs on the auxiliary electrode plate: Ni(OH) 2 +OH - -e - ⁇ NiOOH+ H2O ;
  • the auxiliary electrode plate is an aluminum hydroxide electrode.
  • a reaction occurs on the auxiliary electrode plate: Al(OH) 3 +OH - -e - ⁇ AlO(OH) 2 +H 2 O;
  • Fig. 1 is the flowchart of the method for hydrogen production by electrolysis of water with three-electrode system proposed by an embodiment of the present application;
  • Fig. 2 is the local structure schematic diagram of the electrolyzer of the present application
  • Fig. 3 is the flow chart of the application's assembled electrolyzer
  • Fig. 4 is the schematic diagram of the structure of the electrolytic chamber surrounded by the cathode electrode frame, the retainer and the auxiliary electrode frame provided with the auxiliary electrode plate in the present application;
  • Fig. 5 is a partial structural schematic diagram of Fig. 4 of the present application.
  • Fig. 1 is a flow chart of a method for producing hydrogen by electrolyzing water with a three-electrode system proposed in an embodiment of the present application.
  • Step 1 Assemble the electrolyzer
  • Step 2 form the first circuit between the hydrogen evolution cathode plate 1, the auxiliary electrode plate 2 and the external power supply in the electrolytic cell, and simultaneously form the second circuit between the auxiliary electrode plate 2, the oxygen evolution anode plate 3 and the external power supply, so as to By closing the first circuit and disconnecting the second circuit, a reaction occurs on the hydrogen evolution cathode plate 1: H 2 O+e ⁇ ⁇ 1/2H 2 +OH ⁇ , to prepare hydrogen;
  • Step 3 By opening the first circuit and closing the second circuit, a reaction occurs on the oxygen evolution anode plate 3: OH - -e - ⁇ 1/4O 2 +1/2H 2 O to prepare oxygen , in the same electrolytic cell, connect the three electrodes of the hydrogen evolution cathode plate 1, the auxiliary electrode plate 2 and the oxygen evolution anode plate 3 with the external power supply to form two circuits, and realize the hydrogen gas by controlling the closing and disconnection of the two circuits.
  • the separate preparation of hydrogen and oxygen prevents the mixing of hydrogen and oxygen, which simplifies the cost of separation.
  • the hydrogen evolution cathode plate 1 is connected to the negative pole of the power supply, and the auxiliary electrode plate 2 is connected to the positive pole of the power supply.
  • Hydrogen gas is prepared on the hydrogen evolution cathode plate 1 in the alkaline electrolyte, and the first circuit is electrolyzed in the alkaline electrolyte to obtain hydrogen gas.
  • the auxiliary electrode plate 2 and the oxygen evolution anode plate 3 are electrolyzed to generate oxygen by opening the first circuit and closing the second circuit, that is to say, the auxiliary electrode plate 2 is connected to the negative pole of the power supply, and the oxygen evolution anode plate 3 is connected to The positive pole of the power supply is used to produce oxygen by electrolysis on the oxygen evolution anode plate 3 in the alkaline electrolyte. Since the oxygen evolution anode plate 3 is disconnected during the hydrogen production process, no oxygen will be generated. At the same time, the hydrogen evolution cathode plate 1 is in the process of preparing oxygen. In the off state, hydrogen will not be generated. Therefore, in the process of electrolyzing water, the separate preparation of hydrogen and oxygen can be realized by controlling the on-off of the first circuit and the second circuit. Not only is the operation simple, but also the oxygen and hydrogen are prepared separately, and no oxygen will appear. mixed with hydrogen.
  • the specific process of assembling the electrolyzer is as follows:
  • Step 11 Fix the hydrogen evolution cathode plate 1, the auxiliary electrode plate 2 and the oxygen evolution anode plate 3 on the cathode electrode frame 4, the auxiliary electrode frame 5 and the anode electrode frame 6 respectively, that is to say, on the cathode electrode frame 4, the auxiliary electrode frame Installation holes are opened on frame 5 and anode electrode frame 6 respectively, and then hydrogen evolution cathode plate 1, auxiliary electrode plate 2 and oxygen evolution anode plate 3 are respectively installed on cathode electrode frame 4, auxiliary electrode frame 5 and anode electrode frame 6 in the hole;
  • Step 12 Then seal and install retaining rings 7 between the cathode electrode frame 4 and the auxiliary electrode frame 5 and between the auxiliary electrode frame 5 and the anode electrode frame 6 to obtain a three-electrode assembly.
  • it also includes stacking a plurality of three-electrode assemblies sequentially in the order of the cathode electrode frame 4, the auxiliary electrode frame 5, and the anode electrode frame 6 to form a three-electrode system, specifically, each of the three-electrode assemblies Two adjacent electrode frames 5 are spaced by retaining rings 7, and two adjacent electrode frames between adjacent two three-electrode assemblies are also spaced and compressed by retaining rings 7, for example, there are two three-electrode assemblies At this time, the arrangement between the two three-electrode assemblies is cathode electrode frame 4-retaining ring 7-auxiliary electrode frame 5-retaining ring 7-anode electrode frame 6-retaining ring 7-pole electrode frame 4-retaining ring 7 - the structural arrangement of auxiliary electrode frame 5-retainer ring 7-anode electrode frame 6, in addition, the cathode electrode frame 4, auxiliary electrode frame 5 and retainer ring 7 form an electrolytic chamber, auxiliary electrode frame 5, anode electrode frame 6 The electrolytic chamber that is also surrounded
  • connecting rods are used to sequentially pass through the end pressure plate 8, the insulating plate 9, the cathode electrode frame 4 in the three-electrode system, the auxiliary electrode frame 5, the anode electrode frame 6 and the retaining ring 7, the insulation plate 9 and the end pressure plate After 8, connect the nuts at both ends of the connecting rod, and press them on the two end pressure plates 8 through the nuts, so as to realize the compression and fixation between each electrolytic frame and the retaining ring in the three-electrode system, which can prevent the electrolyte from overflowing.
  • the connecting rod passes through the cathode electrode frame 4-retaining ring 7-auxiliary electrode frame 5-retaining ring 7-anode electrode frame 6-retaining ring 7 - Pole electrode frame 4 - Guard ring 7 - Auxiliary electrode frame 5 - Guard ring 7 - Anode electrode frame 6.
  • the electrolytic cavity enclosed between the cathode electrode frame 4, the auxiliary electrode frame 5 and the retaining ring 7 in each three-electrode assembly in the three-electrode system And the potassium hydroxide electrolyte is passed into the electrolytic cavity enclosed between the auxiliary electrode frame 5, the anode electrode frame 6 and the retaining ring 7, and then an environment for electrolysis is provided.
  • the oxygen or hydrogen generated in the electrolysis chamber flows out through the gas flow hole for collection, that is to say, a connected gas flow hole can be opened on one of the end pressure plates 8 and one of the insulating plates 9, so that the generated hydrogen gas Or oxygen flows out through the gas flow holes for collection. Since the generated oxygen or hydrogen may carry part of the electrolyte during the outflow process, the electrolyte may be lost.
  • one of the end pressure plates 8 and one of the insulating plates 9 Connected liquid flow holes are opened on the top, and then the electrolyte can be passed into the three-electrode assembly through the liquid flow holes, and the electrolyte can enter the electrolysis chamber through the pores of the porous material on the electrode plate of the three-electrode assembly to realize the Electrolyte stability.
  • the hydrogen evolution cathode plate 1 can be one of nickel-based alloy hydrogen evolution electrode, porous nickel hydrogen evolution electrode, nickel-based noble metal oxide hydrogen evolution electrode and nickel-based dispersion composite hydrogen evolution electrode.
  • oxygen evolution anode plate can be an alloy electrode with nickel, cobalt, and iron as effective catalytic components.
  • auxiliary electrode plates 2 there may be various types of auxiliary electrode plates 2 .
  • the auxiliary electrode plate 2 may be a nickel hydroxide electrode.
  • a reaction occurs on the auxiliary electrode plate 2: Ni(OH) 2 + OH ⁇ -e ⁇ ⁇ NiOOH+H 2 O; when the first circuit is opened and the second circuit is closed, a reaction occurs on the auxiliary electrode plate 2: NiOOH+H 2 O+e ⁇ ⁇ Ni(OH) 2 +OH ⁇ .
  • the auxiliary electrode plate 2 can be an aluminum hydroxide electrode.
  • a reaction occurs on the auxiliary electrode plate 2: Al(OH) 3 +OH - -e - ⁇ AlO(OH) 2 +H 2 O;
  • a reaction occurs on the auxiliary electrode plate 2: AlO(OH) 2 +H 2 O+e - ⁇ Al(OH) 3 + OH - .

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Abstract

Provided in the present application is a method for a triple-electrode system electrolyzing water to produce hydrogen. The method comprises the following process: assembling an electrolytic cell; and forming a first circuit between a hydrogen evolution cathode plate, an auxiliary electrode plate and an external power source in the electrolytic cell, and also forming a second circuit between the auxiliary electrode plate, an oxygen evolution anode plate and the external power source, so as to enable, by means of the connection of the first circuit and the disconnection of the second circuit, a reaction on the hydrogen evolution cathode plate to prepare hydrogen, and enable, by means of the disconnection of the first circuit and the connection of the second circuit, a reaction on the oxygen evolution anode plate to prepare oxygen. In the same electrolytic cell, three electrodes, i.e. a hydrogen evolution cathode plate, an auxiliary electrode plate and an oxygen evolution anode plate, and an external power source are connected to form two circuits, such that separate preparation of hydrogen and oxygen is realized by means of controlling the connection and disconnection of the two circuits, and therefore the phenomenon of the mixture of prepared hydrogen and oxygen is avoided, thereby reducing the separation cost.

Description

一种三电极体系电解水制氢方法A method for producing hydrogen by electrolyzing water with a three-electrode system
交叉引用cross reference
本申请要求在2021年11月23日提交中国国家知识产权局、申请号为202111394216.7、发明名称为“一种三电极体系电解水制氢方法”的中国专利申请的优先权,其全部内容通过引用结合在本申请中。This application claims the priority of the Chinese patent application filed with the State Intellectual Property Office of China on November 23, 2021, with the application number 202111394216.7, and the title of the invention is "A method for producing hydrogen by electrolysis of water with a three-electrode system", the entire content of which is incorporated by reference incorporated in this application.
技术领域technical field
本申请涉及电解水制氢技术领域,尤其涉及一种三电极体系电解水制氢方法。The present application relates to the technical field of hydrogen production by electrolysis of water, in particular to a method for hydrogen production by electrolysis of water with a three-electrode system.
背景技术Background technique
现有电解槽是好多个电解室组合在一起,每个电解室的主要组成部分是阴极、阳极、隔膜和电解液。常规的电解水技术在电极过程中阴阳极同时电极生成氢气和氧气,这将很容易导致氢气和氧气的混合,致使所制备的气体不纯,后续的提纯则将大大增大制备成本。采用离子选择性膜隔开在析氢催化电极产生的氢气和析氧催化电极产生的氧气是一种有效的解决方案,但是离子选择性膜的使用也大大增加了成本。此外,由于电化学析氢和析氧自身的动力学过程不同,造成产氢和产氧速度有所差异,当离子选择性膜两边压力不同时,膜的损耗也非常严重,这进一步增大了成本。此外,选择性离子交换膜近一步增大了电解槽内阻,增加了能耗。目前主流的工作在于改进或者制备新型的隔膜,以期降低内阻的同时,又兼顾亲水性,离子透过性以及能够完全隔开氢气和氧气。虽然已经有很多新型隔膜被研究探索,但是效果仍然并不是十分显著。The existing electrolyzer is a combination of many electrolytic chambers, and the main components of each electrolytic chamber are cathode, anode, diaphragm and electrolyte. Conventional water electrolysis technology generates hydrogen and oxygen at the cathode and anode during the electrode process, which will easily lead to the mixing of hydrogen and oxygen, making the prepared gas impure, and the subsequent purification will greatly increase the production cost. Using an ion-selective membrane to separate the hydrogen generated at the hydrogen evolution catalytic electrode and the oxygen generated at the oxygen evolution catalytic electrode is an effective solution, but the use of the ion-selective membrane also greatly increases the cost. In addition, due to the different kinetics of electrochemical hydrogen evolution and oxygen evolution, the rates of hydrogen and oxygen production are different. When the pressure on both sides of the ion-selective membrane is different, the loss of the membrane is also very serious, which further increases the cost. . In addition, the selective ion exchange membrane further increases the internal resistance of the electrolyzer and increases energy consumption. The current mainstream work is to improve or prepare a new type of diaphragm, in order to reduce the internal resistance while taking into account the hydrophilicity, ion permeability and the ability to completely separate hydrogen and oxygen. Although many new diaphragms have been researched and explored, the effect is still not very significant.
发明内容Contents of the invention
本申请旨在至少在一定程度上解决相关技术中的技术问题之一。This application aims to solve one of the technical problems in the related art at least to a certain extent.
为此,本申请的目的在于提出一种三电极体系电解水制氢方法,在同一个电解槽中,将析氢阴极板、辅助电极板和析氧阳极板三个电极与外部电源之间连接成两个电路,通过控制两个电路的闭合和断开实现氢气和氧气的分别制备,进而使得制备的氢气和氧气不会出现混合的现象,简化了分离成本,并且控制方法简单易操作。For this reason, the purpose of this application is to propose a method for producing hydrogen by electrolyzing water with a three-electrode system. The two circuits realize the separate preparation of hydrogen and oxygen by controlling the closing and opening of the two circuits, so that the prepared hydrogen and oxygen will not mix, simplify the separation cost, and the control method is simple and easy to operate.
为达到上述目的,本申请提出的一种三电极体系电解水制氢方法,包括:In order to achieve the above purpose, a method for producing hydrogen by electrolyzing water with a three-electrode system proposed by the present application includes:
组装电解槽;Assemble the electrolyzer;
将电解槽中的析氢阴极板、辅助电极板和外部电源之间组成第一电路,同时将辅助电极板、析氧阳极板和外部电源之间组成第二电路,以通过所述第一电路闭合和所述第二电路断 开使得所述析氢阴极板上发生反应:H 2O+e -→1/2H 2+OH -,制备得到氢气,通过所述第一电路断开和所述第二电路闭合使得所述析氧阳极板上发生反应:OH --e -→1/4O 2+1/2H 2O,制备得到氧气。 A first circuit is formed between the hydrogen evolution cathode plate, the auxiliary electrode plate and the external power supply in the electrolytic cell, and a second circuit is formed between the auxiliary electrode plate, the oxygen evolution anode plate and the external power supply, so as to be closed by the first circuit and the second circuit is disconnected so that a reaction occurs on the hydrogen evolution cathode plate: H 2 O+e - → 1/2H 2 +OH - , hydrogen gas is prepared, and the first circuit is disconnected and the second Closing the circuit causes a reaction to occur on the oxygen evolution anode plate: OH - -e - → 1/4O 2 +1/2H 2 O, and oxygen is produced.
进一步地,所述组装电解槽的具体过程如下:Further, the specific process of the assembled electrolyzer is as follows:
将析氢阴极板、辅助电极板和析氧阳极板分别固定在阴极电极框、辅助电极框和阳极电极框上;Fixing the hydrogen evolution cathode plate, auxiliary electrode plate and oxygen evolution anode plate on the cathode electrode frame, auxiliary electrode frame and anode electrode frame respectively;
然后在阴极电极框和辅助电极框之间以及辅助电极框和阳极电极框之间均密封安装护圈,得到三电极组件。Then, a retaining ring is sealed between the cathode electrode frame and the auxiliary electrode frame and between the auxiliary electrode frame and the anode electrode frame to obtain a three-electrode assembly.
进一步地,还包括将多个三电极组件均按照阴极电极框、辅助电极框、阳极电极框的顺序依次叠加形成三电极体系。Further, it also includes stacking a plurality of three-electrode assemblies sequentially in the order of the cathode electrode frame, the auxiliary electrode frame, and the anode electrode frame to form a three-electrode system.
进一步地,还包括用连接杆依次穿过端压板、绝缘板、三电极体系中的阴极电极框、辅助电极框、阳极电极框和护圈、绝缘板和端压板后,在连接杆的两端连接螺母,通过螺母压紧在两个端压板上。Further, after passing through the end plate, insulating plate, cathode electrode frame in the three-electrode system, auxiliary electrode frame, anode electrode frame and retaining ring, insulating plate and end plate with the connecting rod in sequence, at both ends of the connecting rod The connecting nut is pressed on the two end pressure plates through the nut.
进一步地,还包括通过端压板和绝缘板上的液体流通孔向三电极体系中每个三电极组件中阴极电极框、辅助电极框和护圈之间围成的电解腔以及辅助电极框、阳极电极框和护圈之间围成的电解腔中通入氢氧化钾电解液。Further, it also includes the electrolysis cavity enclosed between the cathode electrode frame, the auxiliary electrode frame and the retaining ring, the auxiliary electrode frame, and the anode in each three-electrode assembly in the three-electrode system through the liquid flow holes on the end pressure plate and the insulating plate. Potassium hydroxide electrolyte is passed into the electrolytic cavity enclosed between the electrode frame and the guard ring.
进一步地,所述析氢阴极板为镍基合金系析氢电极、多孔镍系析氢电极、镍基贵金属氧化物系析氢电极以及镍基弥散复合系析氢电极中的一种。Further, the hydrogen evolution cathode plate is one of nickel-based alloy hydrogen evolution electrode, porous nickel hydrogen evolution electrode, nickel-based noble metal oxide hydrogen evolution electrode and nickel-based dispersion composite hydrogen evolution electrode.
进一步地,所述析氧阳极板为镍、钴、铁为有效催化组分的合金电极。Further, the oxygen evolution anode plate is an alloy electrode with nickel, cobalt, and iron as effective catalytic components.
进一步地,所述辅助电极板为氢氧化镍电极,所述第一电路闭合和所述第二电路断开时,所述辅助电极板上发生反应:Ni(OH) 2+OH --e -→NiOOH+H 2O; Further, the auxiliary electrode plate is a nickel hydroxide electrode. When the first circuit is closed and the second circuit is opened, a reaction occurs on the auxiliary electrode plate: Ni(OH) 2 +OH - -e - →NiOOH+ H2O ;
所述第一电路断开和所述第二电路闭合时,所述辅助电极板上发生反应:NiOOH+H 2O+e -→Ni(OH) 2+OH -When the first circuit is disconnected and the second circuit is closed, a reaction occurs on the auxiliary electrode plate: NiOOH+H 2 O+e →Ni(OH) 2 +OH .
进一步地,所述辅助电极板为氢氧化铝电极,所述第一电路闭合和所述第二电路断开时,所述辅助电极板上发生反应:Al(OH) 3+OH --e -→AlO(OH) 2+H 2O; Further, the auxiliary electrode plate is an aluminum hydroxide electrode. When the first circuit is closed and the second circuit is opened, a reaction occurs on the auxiliary electrode plate: Al(OH) 3 +OH - -e - → AlO(OH) 2 +H 2 O;
所述第一电路断开和所述第二电路闭合时,所述辅助电极板上发生反应:AlO(OH) 2+H 2O+e -→Al(OH) 3+OH -When the first circuit is disconnected and the second circuit is closed, a reaction occurs on the auxiliary electrode plate: AlO(OH) 2 +H 2 O+e →Al(OH) 3 +OH .
本申请附加的方面和优点将在下面的描述中部分给出,部分将从下面的描述中变得明显,或通过本申请的实践了解到。Additional aspects and advantages of the application will be set forth in part in the description which follows, and in part will be obvious from the description, or may be learned by practice of the application.
附图说明Description of drawings
本申请上述的和/或附加的方面和优点从下面结合附图对实施例的描述中将变得明显和 容易理解,其中:The above-mentioned and/or additional aspects and advantages of the present application will become apparent and easy to understand from the following description of the embodiments in conjunction with the accompanying drawings, wherein:
图1是本申请一实施例提出的三电极体系电解水制氢方法的流程图;Fig. 1 is the flowchart of the method for hydrogen production by electrolysis of water with three-electrode system proposed by an embodiment of the present application;
图2是本申请电解槽的局部结构示意图;Fig. 2 is the local structure schematic diagram of the electrolyzer of the present application;
图3是本申请组装电解槽的流程图;Fig. 3 is the flow chart of the application's assembled electrolyzer;
图4是本申请设置有析氢阴极板的阴极电极框、护圈和设置有辅助电极板的辅助电极框之间围成电解腔的结构示意图;Fig. 4 is the schematic diagram of the structure of the electrolytic chamber surrounded by the cathode electrode frame, the retainer and the auxiliary electrode frame provided with the auxiliary electrode plate in the present application;
图5是本申请图4的局部结构示意图;Fig. 5 is a partial structural schematic diagram of Fig. 4 of the present application;
图中:1、析氢阴极板;2、辅助电极板;3、析氧阳极板;4、阴极电极框;5、辅助电极框;6、阳极电极框;7、护圈;8、端压板;9、绝缘板。In the figure: 1, hydrogen evolution cathode plate; 2, auxiliary electrode plate; 3, oxygen evolution anode plate; 4, cathode electrode frame; 5, auxiliary electrode frame; 6, anode electrode frame; 7, retaining ring; 8, end pressure plate; 9. Insulation board.
具体实施方式Detailed ways
下面详细描述本申请的实施例,所述实施例的示例在附图中示出,其中自始至终相同或类似的标号表示相同或类似的元件或具有相同或类似功能的元件。下面通过参考附图描述的实施例是示例性的,仅用于解释本申请,而不能理解为对本申请的限制。相反,本申请的实施例包括落入所附加权利要求书的精神和内涵范围内的所有变化、修改和等同物。Embodiments of the present application are described in detail below, examples of which are shown in the drawings, wherein the same or similar reference numerals denote the same or similar elements or elements having the same or similar functions throughout. The embodiments described below by referring to the figures are exemplary, are only for explaining the present application, and should not be construed as limiting the present application. On the contrary, the embodiments of the present application include all changes, modifications and equivalents falling within the spirit and scope of the appended claims.
图1是本申请一实施例提出的一种三电极体系电解水制氢方法的流程图。Fig. 1 is a flow chart of a method for producing hydrogen by electrolyzing water with a three-electrode system proposed in an embodiment of the present application.
参见图1和图2,一种三电极体系电解水制氢方法,包括如下过程:Referring to Figure 1 and Figure 2, a three-electrode system electrolysis of water hydrogen production method, including the following process:
步骤1:组装电解槽;Step 1: Assemble the electrolyzer;
步骤2:将电解槽中的析氢阴极板1、辅助电极板2和外部电源之间组成第一电路,同时将辅助电极板2、析氧阳极板3和外部电源之间组成第二电路,以通过所述第一电路闭合和所述第二电路断开使得所述析氢阴极板1上发生反应:H 2O+e -→1/2H 2+OH -,制备得到氢气; Step 2: form the first circuit between the hydrogen evolution cathode plate 1, the auxiliary electrode plate 2 and the external power supply in the electrolytic cell, and simultaneously form the second circuit between the auxiliary electrode plate 2, the oxygen evolution anode plate 3 and the external power supply, so as to By closing the first circuit and disconnecting the second circuit, a reaction occurs on the hydrogen evolution cathode plate 1: H 2 O+e →1/2H 2 +OH , to prepare hydrogen;
步骤3:通过所述第一电路断开和所述第二电路闭合使得所述析氧阳极板3上发生反应:OH --e -→1/4O 2+1/2H 2O,制备得到氧气,在同一个电解槽中,将析氢阴极板1、辅助电极板2和析氧阳极板3三个电极与外部电源之间连接成两个电路,通过控制两个电路的闭合和断开实现氢气和氧气的分别制备,进而使得制备的氢气和氧气不会出现混合的现象,简化了分离成本。 Step 3: By opening the first circuit and closing the second circuit, a reaction occurs on the oxygen evolution anode plate 3: OH - -e - → 1/4O 2 +1/2H 2 O to prepare oxygen , in the same electrolytic cell, connect the three electrodes of the hydrogen evolution cathode plate 1, the auxiliary electrode plate 2 and the oxygen evolution anode plate 3 with the external power supply to form two circuits, and realize the hydrogen gas by controlling the closing and disconnection of the two circuits. The separate preparation of hydrogen and oxygen prevents the mixing of hydrogen and oxygen, which simplifies the cost of separation.
详细来说,析氢阴极板1连接电源负极,而辅助电极板2连接电源正极,在碱性电解液中析氢阴极板1上制备得到氢气,实现第一电路在碱性电解液中进行电解得到氢气,当制备氧气时,通过第一电路断开和第二电路闭合使得辅助电极板2和析氧阳极板3电解生成氧气,也就是说,辅助电极板2连接电源负极,析氧阳极板3连接电源正极,在碱性电解液中析氧阳极板3上电解制氧气,由于在氢气制备过程中析氧阳极板3是断开状态,不会生成氧气, 同时制备氧气过程中析氢阴极板1是断开状态,不会生成氢气,因此在电解水过程中通过控制第一电路和第二电路的通断实现氢气和氧气的分开制备,不仅操作简单,并且氧气和氢气分开制备,不会出现氧气和氢气混合的情况。In detail, the hydrogen evolution cathode plate 1 is connected to the negative pole of the power supply, and the auxiliary electrode plate 2 is connected to the positive pole of the power supply. Hydrogen gas is prepared on the hydrogen evolution cathode plate 1 in the alkaline electrolyte, and the first circuit is electrolyzed in the alkaline electrolyte to obtain hydrogen gas. , when oxygen is produced, the auxiliary electrode plate 2 and the oxygen evolution anode plate 3 are electrolyzed to generate oxygen by opening the first circuit and closing the second circuit, that is to say, the auxiliary electrode plate 2 is connected to the negative pole of the power supply, and the oxygen evolution anode plate 3 is connected to The positive pole of the power supply is used to produce oxygen by electrolysis on the oxygen evolution anode plate 3 in the alkaline electrolyte. Since the oxygen evolution anode plate 3 is disconnected during the hydrogen production process, no oxygen will be generated. At the same time, the hydrogen evolution cathode plate 1 is in the process of preparing oxygen. In the off state, hydrogen will not be generated. Therefore, in the process of electrolyzing water, the separate preparation of hydrogen and oxygen can be realized by controlling the on-off of the first circuit and the second circuit. Not only is the operation simple, but also the oxygen and hydrogen are prepared separately, and no oxygen will appear. mixed with hydrogen.
参照图3-5,在一些实施例中,组装电解槽的具体过程如下:3-5, in some embodiments, the specific process of assembling the electrolyzer is as follows:
步骤11:将析氢阴极板1、辅助电极板2和析氧阳极板3分别固定在阴极电极框4、辅助电极框5和阳极电极框6上,也就是说,在阴极电极框4、辅助电极框5和阳极电极框6上分别开设安装孔,然后分别将析氢阴极板1、辅助电极板2和析氧阳极板3安装在阴极电极框4、辅助电极框5和阳极电极框6上的安装孔中;Step 11: Fix the hydrogen evolution cathode plate 1, the auxiliary electrode plate 2 and the oxygen evolution anode plate 3 on the cathode electrode frame 4, the auxiliary electrode frame 5 and the anode electrode frame 6 respectively, that is to say, on the cathode electrode frame 4, the auxiliary electrode frame Installation holes are opened on frame 5 and anode electrode frame 6 respectively, and then hydrogen evolution cathode plate 1, auxiliary electrode plate 2 and oxygen evolution anode plate 3 are respectively installed on cathode electrode frame 4, auxiliary electrode frame 5 and anode electrode frame 6 in the hole;
步骤12:然后在阴极电极框4和辅助电极框5之间以及辅助电极框5和阳极电极框6之间均密封安装护圈7,得到三电极组件。Step 12: Then seal and install retaining rings 7 between the cathode electrode frame 4 and the auxiliary electrode frame 5 and between the auxiliary electrode frame 5 and the anode electrode frame 6 to obtain a three-electrode assembly.
在一些实施例中,还包括将多个三电极组件均按照阴极电极框4、辅助电极框5、阳极电极框6的顺序依次叠加形成三电极体系,具体来说,每个三电极组件中的相邻两个电极框5之间通过护圈7间隔,并且相邻的两个三电极组件之间相近的两个电极框之间也通过护圈7间隔压紧,例如有两个三电极组件时,此时两个三电极组件之间的排布为阴极电极框4-护圈7-辅助电极框5-护圈7-阳极电极框6-护圈7-极电极框4-护圈7-辅助电极框5-护圈7-阳极电极框6的结构排布,另外,阴极电极框4、辅助电极框5和护圈7之间围成电解腔,辅助电极框5、阳极电极框6和护圈7之间也围成的电解腔,两个电解腔中均可以存放电解液,并且由于护圈7与电极框之间密封相接,使得电解腔中存放的电解液不会从电极框与护圈7连接处溢出,由于电极板上的材料通常为多孔结构,因此电解液只能通过电极板上的多孔结构在电解腔之间流动。In some embodiments, it also includes stacking a plurality of three-electrode assemblies sequentially in the order of the cathode electrode frame 4, the auxiliary electrode frame 5, and the anode electrode frame 6 to form a three-electrode system, specifically, each of the three-electrode assemblies Two adjacent electrode frames 5 are spaced by retaining rings 7, and two adjacent electrode frames between adjacent two three-electrode assemblies are also spaced and compressed by retaining rings 7, for example, there are two three-electrode assemblies At this time, the arrangement between the two three-electrode assemblies is cathode electrode frame 4-retaining ring 7-auxiliary electrode frame 5-retaining ring 7-anode electrode frame 6-retaining ring 7-pole electrode frame 4-retaining ring 7 - the structural arrangement of auxiliary electrode frame 5-retainer ring 7-anode electrode frame 6, in addition, the cathode electrode frame 4, auxiliary electrode frame 5 and retainer ring 7 form an electrolytic chamber, auxiliary electrode frame 5, anode electrode frame 6 The electrolytic chamber that is also surrounded by the retaining ring 7 can store electrolyte in the two electrolytic chambers, and because the retaining ring 7 and the electrode frame are sealed and connected, the electrolyte stored in the electrolytic chamber will not flow from the electrode The junction between the frame and the retaining ring 7 overflows, and because the material on the electrode plate is generally porous, the electrolyte can only flow between the electrolytic chambers through the porous structure on the electrode plate.
在一些实施例中,用连接杆依次穿过端压板8、绝缘板9、三电极体系中的阴极电极框4、辅助电极框5、阳极电极框6和护圈7、绝缘板9和端压板8后,在连接杆的两端连接螺母,通过螺母压紧在两个端压板8上,进而实现三电极体系中各个电解框与护圈之间的压紧固定,能够防止电解液的溢出,其中连接杆穿过三电极体系时,以两个三电极组件为例,连接杆依次穿过阴极电极框4-护圈7-辅助电极框5-护圈7-阳极电极框6-护圈7-极电极框4-护圈7-辅助电极框5-护圈7-阳极电极框6。In some embodiments, connecting rods are used to sequentially pass through the end pressure plate 8, the insulating plate 9, the cathode electrode frame 4 in the three-electrode system, the auxiliary electrode frame 5, the anode electrode frame 6 and the retaining ring 7, the insulation plate 9 and the end pressure plate After 8, connect the nuts at both ends of the connecting rod, and press them on the two end pressure plates 8 through the nuts, so as to realize the compression and fixation between each electrolytic frame and the retaining ring in the three-electrode system, which can prevent the electrolyte from overflowing. When the connecting rod passes through the three-electrode system, taking two three-electrode assemblies as an example, the connecting rod passes through the cathode electrode frame 4-retaining ring 7-auxiliary electrode frame 5-retaining ring 7-anode electrode frame 6-retaining ring 7 - Pole electrode frame 4 - Guard ring 7 - Auxiliary electrode frame 5 - Guard ring 7 - Anode electrode frame 6.
在一些实施例中,通过端压板8和绝缘板9上的液体流通孔向三电极体系中每个三电极组件中阴极电极框4、辅助电极框5和护圈7之间围成的电解腔以及辅助电极框5、阳极电极框6和护圈7之间围成的电解腔中通入氢氧化钾电解液,进而提供电解的环境,另外,在端压板8和绝缘板9上均开有气体流通孔,电解腔中生成的氧气或者氢气通过气体流通孔流出进行收集,也就是说,可以在其中一个端压板8和其中一个绝缘板9上开设相连通的气体流通孔,使得生成的氢气或氧气通过气体流通孔流出进行收集,由于生成的氧气或氢气在流 出过程中可能会携带部分电解液,造成电解液可能会有所损失,因此可以在其中一个端压板8和其中一个绝缘板9上均开设相连通的液体流通孔,然后通过液体流通孔可以向三电极组件中通入电解液,电解液可以通过三电极组件上电极板上多孔材料的孔隙进入电解腔中,实现电解腔中电解液的稳定。In some embodiments, through the liquid passage holes on the end pressure plate 8 and the insulating plate 9, the electrolytic cavity enclosed between the cathode electrode frame 4, the auxiliary electrode frame 5 and the retaining ring 7 in each three-electrode assembly in the three-electrode system And the potassium hydroxide electrolyte is passed into the electrolytic cavity enclosed between the auxiliary electrode frame 5, the anode electrode frame 6 and the retaining ring 7, and then an environment for electrolysis is provided. In addition, on the end pressure plate 8 and the insulating plate 9, there are Gas flow hole, the oxygen or hydrogen generated in the electrolysis chamber flows out through the gas flow hole for collection, that is to say, a connected gas flow hole can be opened on one of the end pressure plates 8 and one of the insulating plates 9, so that the generated hydrogen gas Or oxygen flows out through the gas flow holes for collection. Since the generated oxygen or hydrogen may carry part of the electrolyte during the outflow process, the electrolyte may be lost. Therefore, one of the end pressure plates 8 and one of the insulating plates 9 Connected liquid flow holes are opened on the top, and then the electrolyte can be passed into the three-electrode assembly through the liquid flow holes, and the electrolyte can enter the electrolysis chamber through the pores of the porous material on the electrode plate of the three-electrode assembly to realize the Electrolyte stability.
在一些实施例中,析氢阴极板1可以为镍基合金系析氢电极、多孔镍系析氢电极、镍基贵金属氧化物系析氢电极以及镍基弥散复合系析氢电极中的一种。In some embodiments, the hydrogen evolution cathode plate 1 can be one of nickel-based alloy hydrogen evolution electrode, porous nickel hydrogen evolution electrode, nickel-based noble metal oxide hydrogen evolution electrode and nickel-based dispersion composite hydrogen evolution electrode.
另外,析氧阳极板可以为镍、钴、铁为有效催化组分的合金电极。In addition, the oxygen evolution anode plate can be an alloy electrode with nickel, cobalt, and iron as effective catalytic components.
需要详细说明的是,辅助电极板2的种类可以有多种。It should be explained in detail that there may be various types of auxiliary electrode plates 2 .
作为一种可能的情况,辅助电极板2可以为氢氧化镍电极,此时,当第一电路闭合和所述第二电路断开时,辅助电极板2上发生反应:Ni(OH) 2+OH --e -→NiOOH+H 2O;第一电路断开和第二电路闭合时,辅助电极板2上发生反应:NiOOH+H 2O+e -→Ni(OH) 2+OH -As a possible situation, the auxiliary electrode plate 2 may be a nickel hydroxide electrode. At this time, when the first circuit is closed and the second circuit is disconnected, a reaction occurs on the auxiliary electrode plate 2: Ni(OH) 2 + OH -e →NiOOH+H 2 O; when the first circuit is opened and the second circuit is closed, a reaction occurs on the auxiliary electrode plate 2: NiOOH+H 2 O+e →Ni(OH) 2 +OH .
作为另一种可能的情况,辅助电极板2可以为氢氧化铝电极,第一电路闭合和第二电路断开时,辅助电极板2上发生反应:Al(OH) 3+OH --e -→AlO(OH) 2+H 2O;第一电路断开和第二电路闭合时,辅助电极板2上发生反应:AlO(OH) 2+H 2O+e -→Al(OH) 3+OH -As another possible situation, the auxiliary electrode plate 2 can be an aluminum hydroxide electrode. When the first circuit is closed and the second circuit is disconnected, a reaction occurs on the auxiliary electrode plate 2: Al(OH) 3 +OH - -e - →AlO(OH) 2 +H 2 O; when the first circuit is opened and the second circuit is closed, a reaction occurs on the auxiliary electrode plate 2: AlO(OH) 2 +H 2 O+e - →Al(OH) 3 + OH - .
需要说明的是,在本申请的描述中,术语“第一”、“第二”等仅用于描述目的,而不能理解为指示或暗示相对重要性。此外,在本申请的描述中,除非另有说明,“多个”的含义是两个或两个以上。It should be noted that, in the description of the present application, terms such as "first" and "second" are used for description purposes only, and should not be understood as indicating or implying relative importance. In addition, in the description of the present application, unless otherwise specified, "plurality" means two or more.
流程图中或在此以其他方式描述的任何过程或方法描述可以被理解为,表示包括一个或更多个用于实现特定逻辑功能或过程的步骤的可执行指令的代码的模块、片段或部分,并且本申请的可选实施方式的范围包括另外的实现,其中可以不按所示出或讨论的顺序,包括根据所涉及的功能按基本同时的方式或按相反的顺序,来执行功能,这应被本申请的实施例所属技术领域的技术人员所理解。Any process or method descriptions in flowcharts or otherwise described herein may be understood to represent modules, segments or portions of code comprising one or more executable instructions for implementing specific logical functions or steps of the process , and the scope of alternative embodiments of the present application includes additional implementations in which functions may be performed out of the order shown or discussed, including substantially concurrently or in reverse order depending upon the functions involved, which It should be understood by those skilled in the art to which the embodiments of the present application belong.
在本说明书的描述中,参考术语“一个实施例”、“一些实施例”、“示例”、“具体示例”、或“一些示例”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申请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 referring to the terms "one embodiment", "some embodiments", "example", "specific examples", or "some examples" mean that specific features described in connection with the embodiment or example , structure, material or characteristic is included in at least one embodiment or example of the present application. 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.
尽管上面已经示出和描述了本申请的实施例,可以理解的是,上述实施例是示例性的,不能理解为对本申请的限制,本领域的普通技术人员在本申请的范围内可以对上述实施例进行变化、修改、替换和变型。Although the embodiments of the present application have been shown and described above, it can be understood that the above embodiments are exemplary and should not be construed as limitations on the present application, and those skilled in the art can make the above-mentioned The embodiments are subject to changes, modifications, substitutions and variations.

Claims (9)

  1. 一种三电极体系电解水制氢方法,其特征在于,包括:A method for producing hydrogen by electrolyzing water with a three-electrode system, characterized in that it comprises:
    组装电解槽;Assemble the electrolyzer;
    将电解槽中的析氢阴极板、辅助电极板和外部电源之间组成第一电路,同时将辅助电极板、析氧阳极板和外部电源之间组成第二电路,以通过所述第一电路闭合和所述第二电路断开使得所述析氢阴极板上发生反应:H 2O+e -→1/2H 2+OH -,制备得到氢气,通过所述第一电路断开和所述第二电路闭合使得所述析氧阳极板上发生反应:OH --e -→1/4O 2+1/2H 2O,制备得到氧气。 A first circuit is formed between the hydrogen evolution cathode plate, the auxiliary electrode plate and the external power supply in the electrolytic cell, and a second circuit is formed between the auxiliary electrode plate, the oxygen evolution anode plate and the external power supply, so as to be closed by the first circuit and the second circuit is disconnected so that a reaction occurs on the hydrogen evolution cathode plate: H 2 O+e - → 1/2H 2 +OH - , hydrogen gas is prepared, and the first circuit is disconnected and the second Closing the circuit causes a reaction to occur on the oxygen evolution anode plate: OH - -e - → 1/4O 2 +1/2H 2 O, and oxygen is produced.
  2. 如权利要求1所述的三电极体系电解水制氢方法,其特征在于,所述组装电解槽的具体过程如下:The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 1, wherein the specific process of assembling the electrolyzer is as follows:
    将析氢阴极板、辅助电极板和析氧阳极板分别固定在阴极电极框、辅助电极框和阳极电极框上;Fixing the hydrogen evolution cathode plate, auxiliary electrode plate and oxygen evolution anode plate on the cathode electrode frame, auxiliary electrode frame and anode electrode frame respectively;
    然后在阴极电极框和辅助电极框之间以及辅助电极框和阳极电极框之间均密封安装护圈,得到三电极组件。Then, a retaining ring is sealed between the cathode electrode frame and the auxiliary electrode frame and between the auxiliary electrode frame and the anode electrode frame to obtain a three-electrode assembly.
  3. 如权利要求2所述的三电极体系电解水制氢方法,其特征在于,还包括将多个三电极组件均按照阴极电极框、辅助电极框、阳极电极框的顺序依次叠加形成三电极体系。The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 2, further comprising stacking a plurality of three-electrode assemblies sequentially in the order of a cathode electrode frame, an auxiliary electrode frame, and an anode electrode frame to form a three-electrode system.
  4. 如权利要求3所述的三电极体系电解水制氢方法,其特征在于,还包括:The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 3, further comprising:
    用连接杆依次穿过端压板、绝缘板、三电极体系中的阴极电极框、辅助电极框、阳极电极框和护圈、绝缘板和端压板后,在连接杆的两端连接螺母,通过螺母压紧在两个端压板上。Use the connecting rod to pass through the end pressure plate, insulating plate, cathode electrode frame, auxiliary electrode frame, anode electrode frame and retaining ring, insulating plate and end pressure plate in the three-electrode system in sequence, and connect nuts at both ends of the connecting rod, and pass the nut Compressed on both end platens.
  5. 如权利要求4所述的三电极体系电解水制氢方法,其特征在于,还包括通过端压板和绝缘板上的液体流通孔向三电极体系中每个三电极组件中阴极电极框、辅助电极框和护圈之间围成的电解腔以及辅助电极框、阳极电极框和护圈之间围成的电解腔中通入氢氧化钾电解液。The method for producing hydrogen by electrolysis of water in a three-electrode system according to claim 4, further comprising feeding the cathode electrode frame and the auxiliary electrode in each three-electrode assembly in the three-electrode system through the liquid flow holes on the end pressure plate and the insulating plate Potassium hydroxide electrolyte is passed into the electrolytic cavity enclosed between the frame and the retaining ring and the electrolytic cavity enclosed between the auxiliary electrode frame, the anode electrode frame and the retaining ring.
  6. 如权利要求1所述的三电极体系电解水制氢方法,其特征在于,所述析氢阴极板为镍基合金系析氢电极、多孔镍系析氢电极、镍基贵金属氧化物系析氢电极以及镍基弥散复合 系析氢电极中的一种。The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 1, wherein the hydrogen-evolving cathode plate is a nickel-based alloy-based hydrogen-evolving electrode, a porous nickel-based hydrogen-evolving electrode, a nickel-based noble metal oxide-based hydrogen-evolving electrode, and a nickel-based One of the hydrogen evolution electrodes of the dispersion composite system.
  7. 如权利要求1所述的三电极体系电解水制氢方法,其特征在于,所述析氧阳极板为镍、钴、铁为有效催化组分的合金电极。The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 1, wherein the oxygen-evolving anode plate is an alloy electrode in which nickel, cobalt, and iron are effective catalytic components.
  8. 如权利要求1所述的三电极体系电解水制氢方法,其特征在于,所述辅助电极板为氢氧化镍电极,所述第一电路闭合和所述第二电路断开时,所述辅助电极板上发生反应:Ni(OH) 2+OH --e -→NiOOH+H 2O; The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 1, wherein the auxiliary electrode plate is a nickel hydroxide electrode, and when the first circuit is closed and the second circuit is disconnected, the auxiliary electrode plate A reaction occurs on the electrode plate: Ni(OH) 2 +OH - -e - →NiOOH+H 2 O;
    所述第一电路断开和所述第二电路闭合时,所述辅助电极板上发生反应:NiOOH+H 2O+e -→Ni(OH) 2+OH -When the first circuit is disconnected and the second circuit is closed, a reaction occurs on the auxiliary electrode plate: NiOOH+H 2 O+e →Ni(OH) 2 +OH .
  9. 如权利要求1所述的三电极体系电解水制氢方法,其特征在于,所述辅助电极板为氢氧化铝电极,所述第一电路闭合和所述第二电路断开时,所述辅助电极板上发生反应:Al(OH) 3+OH --e -→AlO(OH) 2+H 2O; The method for producing hydrogen by electrolyzing water with a three-electrode system according to claim 1, wherein the auxiliary electrode plate is an aluminum hydroxide electrode, and when the first circuit is closed and the second circuit is disconnected, the auxiliary A reaction occurs on the electrode plate: Al(OH) 3 +OH - -e - →AlO(OH) 2 +H 2 O;
    所述第一电路断开和所述第二电路闭合时,所述辅助电极板上发生反应:AlO(OH) 2+H 2O+e -→Al(OH) 3+OH -When the first circuit is disconnected and the second circuit is closed, a reaction occurs on the auxiliary electrode plate: AlO(OH) 2 +H 2 O+e →Al(OH) 3 +OH .
PCT/CN2022/099672 2021-11-23 2022-06-20 Method for triple-electrode system electrolyzing water to produce hydrogen WO2023093012A1 (en)

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