[go: up one dir, main page]

CN115646191A - Hydrogen separation device and method of use based on nickel-BZNY proton conductor - Google Patents

Hydrogen separation device and method of use based on nickel-BZNY proton conductor Download PDF

Info

Publication number
CN115646191A
CN115646191A CN202211400552.2A CN202211400552A CN115646191A CN 115646191 A CN115646191 A CN 115646191A CN 202211400552 A CN202211400552 A CN 202211400552A CN 115646191 A CN115646191 A CN 115646191A
Authority
CN
China
Prior art keywords
bzny
proton conductor
hydrogen
lead
insulating sleeve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN202211400552.2A
Other languages
Chinese (zh)
Other versions
CN115646191B (en
Inventor
罗天勇
蒋元鑫
覃凯煜
廖颖晴
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lingtian Technology Huzhou Co ltd
Original Assignee
University of Electronic Science and Technology of China
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by University of Electronic Science and Technology of China filed Critical University of Electronic Science and Technology of China
Priority to CN202211400552.2A priority Critical patent/CN115646191B/en
Publication of CN115646191A publication Critical patent/CN115646191A/en
Application granted granted Critical
Publication of CN115646191B publication Critical patent/CN115646191B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin
    • Y02E30/10Nuclear fusion reactors

Landscapes

  • Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)

Abstract

The invention discloses hydrogen separation equipment based on a nickel-BZNY proton conductor and a using method thereof, wherein the equipment comprises the following steps: a BZNY proton conductor; the first metal nickel electrode and the second metal nickel electrode are respectively arranged on two sides of the BZNY proton conductor; the conductive end of the first lead is connected with the first metal nickel electrode; the conductive end of the second lead is connected with the second metal nickel electrode; the access end of the first lead and the access end of the second lead are both connected with external electric signal input equipment; a first insulating sleeve having a hydrogen gas extraction space formed therein; the second insulating sleeve is sleeved outside the first insulating sleeve, and a hydrogen-containing mixed gas providing space is formed between the second insulating sleeve and the first insulating sleeve. The invention adopts metal nickel as an electrode, the voltage required by the operation under the ultra-low concentration can be less than 10V, the precipitation phenomenon of nickel can not be induced almost, and meanwhile, the cathode and the anode adopt the same material, thereby simplifying the processing technology of the diaphragm.

Description

基于镍-BZNY质子导体的氢分离设备和使用方法Hydrogen separation device and method of use based on nickel-BZNY proton conductor

技术领域technical field

本发明涉及氢分离领域,尤其涉及基于镍-BZNY质子导体的氢分离设备和使用方法。The invention relates to the field of hydrogen separation, in particular to a nickel-BZNY proton conductor-based hydrogen separation device and usage method.

背景技术Background technique

核聚变被普遍认为是人类能源的终极解决方案,其基本原理是高温下发生聚变反应,氢的同位素氘和氚结合生成较重原子核如氦,同时放出巨大能量。在聚变反应产物的氦会混有一定量的氢同位素,需要将氢同位素与聚变产物氦进行分离提纯。另外,为了保证聚变堆燃料循环系统的氚自持,需要以氦气作为载气,利用聚变反应产生的中子对包层中的锂原子核进行轰击从而产氚,产生的氚需要被带出从而进一步进行氚回收,在该过程中同样涉及到氢同位素与氦的分离问题。Nuclear fusion is generally considered to be the ultimate solution to human energy. Its basic principle is that fusion reactions occur at high temperatures, and hydrogen isotopes deuterium and tritium combine to form heavier nuclei such as helium, and at the same time release huge energy. There will be a certain amount of hydrogen isotope mixed in the helium of the fusion reaction product, which needs to be separated and purified from the fusion product helium. In addition, in order to ensure the self-sustainability of tritium in the fuel cycle system of the fusion reactor, it is necessary to use helium as the carrier gas, and use the neutrons generated by the fusion reaction to bombard the lithium nuclei in the cladding to produce tritium, and the tritium produced needs to be taken out for further Tritium recovery is carried out, which also involves the separation of hydrogen isotopes and helium.

现有解决氢同位素与氦分离的办法主要采用生冷分离技术,即通过利用氢氦沸点(分别是77K和4K左右)不同的特性完成分离过程,即当温度降低到77K以下时,氢同位素气体开始凝结成液相,吸附在特制的吸附柱上,而氦气仍在沸点温度以上,仅发生较小凝结,从而实现氢同位素与氦的分离。上述方式的缺点在于能耗过高、系统复杂以及吸附效率低,其他混合气体也可能发生凝结吸附从而导致分离所得的氢同位素气体纯度不高,后续还有多次纯化工序。采用生冷分离技术分离提取氢同位素时,由于聚变反应产物和载气的工况温度较高,载气还需要从77K以下重新加热到高温,一方面能耗经济性比较差,另一方面由于分离前后系统温差较大,对结构设计以及结构材料的选择带来了一定困难。The existing solution to the separation of hydrogen isotopes and helium mainly adopts the separation technology of raw and cold, that is, the separation process is completed by utilizing the different characteristics of the boiling points of hydrogen and helium (about 77K and 4K respectively), that is, when the temperature drops below 77K, the hydrogen isotope gas begins to It condenses into a liquid phase and is adsorbed on a special adsorption column, while the helium is still above the boiling point temperature, only a small condensation occurs, thereby realizing the separation of hydrogen isotopes and helium. The disadvantages of the above method are high energy consumption, complex system, and low adsorption efficiency. Other mixed gases may also undergo condensation and adsorption, resulting in low purity of the separated hydrogen isotope gas, and multiple subsequent purification processes. When the separation and extraction of hydrogen isotopes is carried out using raw-cooling separation technology, due to the high temperature of the fusion reaction product and the carrier gas, the carrier gas needs to be reheated from below 77K to a high temperature. The temperature difference between the front and rear systems is large, which brings certain difficulties to the structural design and the selection of structural materials.

为了提高氢同位素与氦分离的能耗经济性,近几年在基于钡锆氧化物(BZ)、钡锆钇氧化物(BZY)的透氢特性上,开发出了以BaZrxCeyY1-x-yO3-δ或BaZrxY1-xO3-δ为质子导体电解质、采用氧化物电极(NiO-NiO-BaZrxY1-xO3-δ或NiO-BaZrxCeyY1-x-yO3-δ作为阳极,LaxSr1- xCoyFe1-yO3-δ或LaxSr1-xMnO3-δ作为阴极)的氢氦分离设备及其制备工艺,例如申请号为CN201910919469.8的发明专利以及申请号为CN201910919470.0的发明专利。In order to improve the energy consumption economy of the separation of hydrogen isotopes and helium, based on the hydrogen permeability characteristics of barium zirconium oxide (BZ) and barium zirconium yttrium oxide (BZY) in recent years, BaZr x Ce y Y 1 -xy O 3-δ or BaZr x Y 1-x O 3-δ is the proton conductor electrolyte, using oxide electrodes (NiO-NiO-BaZr x Y 1-x O 3-δ or NiO-BaZr x Ce y Y 1 -xy O 3-δ as the anode, La x Sr 1- x Co y Fe 1-y O 3-δ or La x Sr 1-x MnO 3-δ as the cathode) hydrogen-helium separation equipment and its preparation process, for example The invention patent with application number CN201910919469.8 and the invention patent with application number CN201910919470.0.

在实际的使用研究过程中,当采用如上所示的氧化物电极时,在超低氢浓度下(含氢混合气体的氢气含量低于0.001%)完成氢氦分离过程需要提供超过100伏的电压,极大限制了其后续的工程化应用。In the actual use research process, when using the oxide electrode as shown above, it is necessary to provide a voltage of more than 100 volts to complete the hydrogen-helium separation process at an ultra-low hydrogen concentration (the hydrogen content of the hydrogen-containing mixed gas is less than 0.001%) , which greatly limits its subsequent engineering application.

同时,由于阴极材料、阳极材料不同,使得阴阳两级在实际加工工艺上,需要根据各自材料的烧结特性进行工艺与性能的权衡:若为了工艺,采用与质子导体实现稳固结合的烧结温度存在较大差异时,会导致氧化物电极和质子导体出现明显的界面弱结合问题,易发生膜层脱落现象;反之,则会使得加工工艺非常复杂。At the same time, due to the different cathode materials and anode materials, in the actual processing technology of the cathode and anode, it is necessary to balance the technology and performance according to the sintering characteristics of their respective materials: if it is for the sake of technology, it is difficult to use the sintering temperature to achieve a stable combination with the proton conductor. When the difference is large, it will lead to obvious interface weak bonding between the oxide electrode and the proton conductor, and the phenomenon of film layer peeling will easily occur; otherwise, the processing technology will be very complicated.

发明内容Contents of the invention

本发明的目的在于克服现有技术的不足,提供基于镍-BZNY质子导体的氢分离设备和使用方法。The purpose of the present invention is to overcome the deficiencies of the prior art, and provide hydrogen separation equipment and using methods based on nickel-BZNY proton conductors.

本发明的目的是通过以下技术方案来实现的:The purpose of the present invention is achieved through the following technical solutions:

本发明的第一方面,提供一种基于镍-BZNY质子导体的氢分离设备,包括:The first aspect of the present invention provides a kind of hydrogen separation equipment based on nickel-BZNY proton conductor, comprising:

BZNY质子导体;BZNY proton conductor;

第一金属镍电极和第二金属镍电极,分别设置于BZNY质子导体两侧;The first metal nickel electrode and the second metal nickel electrode are respectively arranged on both sides of the BZNY proton conductor;

第一引线,导电端与第一金属镍电极连接;第二引线,导电端与第二金属镍电极连接;第一引线的接入端和第二引线的接入端均与外部电信号输入设备连接;The first lead wire, the conductive end is connected to the first metal nickel electrode; the second lead wire, the conductive end is connected to the second metal nickel electrode; the access end of the first lead wire and the access end of the second lead wire are connected to the external electrical signal input device connect;

第一绝缘套筒,连接在BZNY质子导体位于第一金属镍电极的一侧并套设在第一金属镍电极的外围,第一绝缘套筒内部形成氢气提取空间;The first insulating sleeve is connected to the side of the BZNY proton conductor located on the first metal nickel electrode and sleeved on the periphery of the first metal nickel electrode, and a hydrogen extraction space is formed inside the first insulating sleeve;

第二绝缘套筒,套设在第一绝缘套筒外侧,与第一绝缘套筒之间形成含氢混合气体提供空间。The second insulating sleeve is sleeved on the outside of the first insulating sleeve, and forms a hydrogen-containing mixed gas supply space with the first insulating sleeve.

进一步地,第一引线的导电端通过烧结、焊接、沉积、热压或冷压的方式与第一金属镍电极连接,第二引线的导电端通过烧结、焊接、沉积、热压或冷压的方式与第二金属镍电极连接。Further, the conductive end of the first lead is connected to the first metal nickel electrode by sintering, welding, deposition, hot pressing or cold pressing, and the conductive end of the second lead is connected by sintering, welding, deposition, hot pressing or cold pressing. The way is connected with the second metal nickel electrode.

进一步地,所述的第一绝缘套筒为耐高温陶瓷管,所述第二绝缘套筒为耐高温玻璃管。Further, the first insulating sleeve is a high temperature resistant ceramic tube, and the second insulating sleeve is a high temperature resistant glass tube.

进一步地,所述含氢混合气体的氢气含量低于0.001%。Further, the hydrogen content of the hydrogen-containing mixed gas is lower than 0.001%.

进一步地,所述外部电信号输入设备输入的电信号,输入曲线的变电压大小范围在-10V至10V区间,恒电压大小范围在1-10V。Further, for the electrical signal input by the external electrical signal input device, the variable voltage of the input curve ranges from -10V to 10V, and the constant voltage ranges from 1-10V.

进一步地,所述BZNY质子导体的最终烧结温度范围在1200-1600摄氏度。Further, the final sintering temperature range of the BZNY proton conductor is 1200-1600 degrees Celsius.

进一步地,所述第一引线和第二引线均为高纯度银线。Further, both the first lead wire and the second lead wire are high-purity silver wires.

进一步地,金属镍电极的制作的方法包含电镀法、溅射法、还原法、气相沉积法。Further, the method of making metal nickel electrodes includes electroplating method, sputtering method, reduction method and vapor phase deposition method.

进一步地,所述第一金属镍电极和第二金属镍电极的厚度为10-1000nm,第一引线和第二引线的直径为0.2-0.6mm。Further, the thickness of the first metal nickel electrode and the second metal nickel electrode is 10-1000 nm, and the diameter of the first lead wire and the second lead wire is 0.2-0.6 mm.

本发明的第二方面,提供所述的基于镍-BZNY质子导体的氢分离设备的使用方法,包括以下步骤:A second aspect of the present invention provides the method for using the hydrogen separation device based on the nickel-BZNY proton conductor, comprising the following steps:

将含氢混合气体通入第二绝缘套筒;Pass the hydrogen-containing mixed gas into the second insulating sleeve;

第一金属镍电极通过第一引线接收外部电信号,同时第二金属镍电极通过第二引线接收外部信号;The first metal nickel electrode receives an external electrical signal through the first lead, while the second metal nickel electrode receives the external signal through the second lead;

含氢混合气体的氢同位素在电信号的控制下,通过BZNY质子导体被抽取到第一绝缘套筒的氢气提取空间。The hydrogen isotope of the hydrogen-containing mixed gas is extracted to the hydrogen extraction space of the first insulating sleeve through the BZNY proton conductor under the control of the electric signal.

本发明的有益效果是:The beneficial effects of the present invention are:

(1)在本发明的一示例性实施例中,采用金属镍作为电极,因氢在镍中具有一定的溶解度,镍电极有利于超低浓度氢的渗入以完成后续的氢分离过程,且采用金属电极可以降低氢分离过程所需的给定电信号输入的工作电压。镍金属电极在超低浓度下工作所需的电压可小于10V且几乎不会诱发镍的析出现象。同时,呈现膜片中心对称结构,阴极和阳极采用同种材料,简化了膜片加工工艺,规避了现有技术中采用氧化物电极由于阴阳极材料不同、在实际加工工艺上需要根据各自材料的烧结特性进行工艺与性能权衡的困境。采用BZNY材料作为质子导体,镍元素的添加有利于质子导体的致密化和烧结温度的降低,进一步即降低能耗成本和对烧结炉设备的要求。另外,BZNY质子导体因成分中含有部分镍,与金属镍电极具有更好的兼容性和界面结合力,解决了氧化物电极膜易于从质子导体层脱落的难题。(1) In an exemplary embodiment of the present invention, metal nickel is used as the electrode, because hydrogen has a certain solubility in nickel, and the nickel electrode is conducive to the infiltration of ultra-low concentration hydrogen to complete the subsequent hydrogen separation process, and adopts Metal electrodes can reduce the operating voltage required for a given electrical signal input to the hydrogen separation process. The voltage required for the nickel metal electrode to work at an ultra-low concentration can be less than 10V and hardly induce the precipitation of nickel. At the same time, it presents a central symmetrical structure of the diaphragm, and the cathode and anode are made of the same material, which simplifies the diaphragm processing technology and avoids the use of oxide electrodes in the prior art due to the different materials of the cathode and anode. Difficulties in the trade-off between process and performance of sintering characteristics. The BZNY material is used as the proton conductor, and the addition of nickel element is beneficial to the densification of the proton conductor and the reduction of the sintering temperature, which further reduces the energy consumption cost and the requirements for the sintering furnace equipment. In addition, because the BZNY proton conductor contains some nickel in its composition, it has better compatibility and interfacial bonding with the metal nickel electrode, which solves the problem that the oxide electrode film is easy to fall off from the proton conductor layer.

(2)在本发明的又一示例性实施例中,当金属镍电极制作的方法采用的磁控溅射工艺时,相比氧化物电极采用的涂敷+烧结工艺,可以提升界面结合力,提高电极的膜层均匀性和工艺的成熟可靠性。因氧化物电极采用涂敷技术,其界面结合力低,在实际工作几十个小时后易发生膜层分离和脱落现象,而采用磁控溅射制备的金属镍电极在长达百小时的反复实验未发现电极和电解质的膜层分离和现象,且长时工作下的镍-BZNY质子导体元件的氢分离性能未发现明显波动。(2) In another exemplary embodiment of the present invention, when the magnetron sputtering process adopted in the method for making the metal nickel electrode, compared with the coating + sintering process adopted by the oxide electrode, the interface bonding force can be improved, Improve the uniformity of the film layer of the electrode and the mature reliability of the process. Because the oxide electrode adopts coating technology, its interfacial bonding force is low, and the film layer separation and shedding are prone to occur after dozens of hours of actual work. The experiment did not find the membrane layer separation and phenomenon of the electrode and the electrolyte, and the hydrogen separation performance of the nickel-BZNY proton conductor element under long-term work did not find obvious fluctuations.

(3)在本发明的又一示例性实施例中,采用镍金属电极,相比氧化物电极更适用使用银制引线实现连接,提高设备层面引线封装互连工艺的可靠性。(3) In yet another exemplary embodiment of the present invention, nickel metal electrodes are used, which are more suitable for connection with silver leads than oxide electrodes, so as to improve the reliability of the device-level lead packaging interconnection process.

附图说明Description of drawings

图1为本发明一示例性实施例提供的基于镍-BZNY质子导体的氢分离设备的结构示意图;Fig. 1 is the structural representation of the hydrogen separation equipment based on nickel-BZNY proton conductor provided by an exemplary embodiment of the present invention;

图2a为本发明一示例性实施例中提供的使用射频磁控溅射技术生长的金属镍电极的X射线衍射图;Fig. 2 a is the X-ray diffraction pattern of the metal nickel electrode grown using radio frequency magnetron sputtering technology provided in an exemplary embodiment of the present invention;

图2b为本发明一示例性实施例中提供的BZNY质子导体的X射线衍射图;Figure 2b is an X-ray diffraction pattern of the BZNY proton conductor provided in an exemplary embodiment of the present invention;

图3a为本发明一示例性实施例中提供的射频磁控溅射的金属镍电极截面的扫描电子显微镜图;Fig. 3 a is the scanning electron micrograph of the metal nickel electrode section of the radio frequency magnetron sputtering provided in an exemplary embodiment of the present invention;

图3b为本发明一示例性实施例中提供的BZNY质子导体截面的扫描电子显微镜图;Figure 3b is a scanning electron microscope image of the BZNY proton conductor section provided in an exemplary embodiment of the present invention;

图4为本发明一示例性实施例中提供的一种基于镍-BZNY质子导体元件的样品图;Fig. 4 is a kind of sample figure based on nickel-BZNY proton conductor element provided in an exemplary embodiment of the present invention;

图5为本发明一示例性实施例中提供的从氢含量为0.001%的氢氦混合气体中提取氢气时、以电压形式提供的给定电信号输入与氢透过率之间的关系示意图。5 is a schematic diagram of the relationship between a given electrical signal input in the form of voltage and hydrogen transmission rate when extracting hydrogen from a hydrogen-helium mixed gas with a hydrogen content of 0.001% provided in an exemplary embodiment of the present invention.

图中,1-BZNY质子导体,201-第一金属镍电极,202-第二金属镍电极,301-第一引线,302-第二引线,4-外部电信号输入设备,501-第一绝缘套筒,50101-氢气提取空间,502-第二绝缘套筒,50201-含氢混合气体提供空间,6-连接点。In the figure, 1-BZNY proton conductor, 201-first metal nickel electrode, 202-second metal nickel electrode, 301-first lead wire, 302-second lead wire, 4-external electrical signal input device, 501-first insulation Sleeve, 50101-hydrogen extraction space, 502-second insulating sleeve, 50201-hydrogen-containing mixed gas supply space, 6-connection point.

具体实施方式Detailed ways

下面结合附图对本发明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。The technical solutions of the present invention will be clearly and completely described below in conjunction with the accompanying drawings. Apparently, the described embodiments are part of the embodiments of the present invention, but 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.

在本发明的描述中,需要说明的是,属于“中心”、“上”、“下”、“左”、“右”、“竖直”、“水平”、“内”、“外”等指示的方向或位置关系为基于附图所述的方向或位置关系,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装置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。此外,属于“第一”、“第二”仅用于描述目的,而不能理解为指示或暗示相对重要性。In the description of the present invention, it should be noted that the terms belonging to "center", "upper", "lower", "left", "right", "vertical", "horizontal", "inner", "outer" etc. The indicated direction or positional relationship is based on the direction or positional relationship described in the drawings, and is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, or in a specific orientation. construction and operation, therefore, should not be construed as limiting the invention. In addition, belonging to "first" and "second" is only for descriptive purposes, and should not be understood as indicating or implying relative importance.

在本发明的描述中,需要说明的是,除非另有明确的规定和限定,属于“安装”、“相连”、“连接”应做广义理解,例如,可以是固定连接,也可以是可拆卸连接,或一体地连接;可以是机械连接,也可以是电连接;可以是直接相连,也可以通过中间媒介间接相连,可以是两个元件内部的连通。对于本领域的普通技术人员而言,可以具体情况理解上述术语在本发明中的具体含义。In the description of the present invention, it should be noted that, unless otherwise specified and limited, "installation", "connection" and "connection" should be understood in a broad sense, for example, it can be a fixed connection or a detachable connection. Connected, or integrally connected; it may be mechanically connected or electrically connected; it may be directly connected or indirectly connected through an intermediary, and it may be the internal communication of two components. Those of ordinary skill in the art can understand the specific meanings of the above terms in the present invention in specific situations.

此外,下面所描述的本发明不同实施方式中所涉及的技术特征只要彼此之间未构成冲突就可以相互结合。In addition, the technical features involved in the different embodiments of the present invention described below may be combined with each other as long as there is no conflict with each other.

下述内容将先对技术名词做解释:The following content will first explain the technical terms:

质子导体:质子导体是指能传导氢离子的固体电解质,又称氢离子导体。质子在固体中的传导可分为两类:一类是在具有氢键的化合物中的传导;另一类是在没有氢键的化合物中的传导。已知的质子导体大部分具有氢键,它们的传导机理是通过氢离子的跃迁并伴随着分子的转动。Proton conductor: A proton conductor refers to a solid electrolyte that can conduct hydrogen ions, also known as a hydrogen ion conductor. The conduction of protons in solids can be divided into two categories: one is conduction in compounds with hydrogen bonds; the other is conduction in compounds without hydrogen bonds. Most of the known proton conductors have hydrogen bonds, and their conduction mechanism is through the transition of hydrogen ions accompanied by the rotation of molecules.

BZNY质子导体:作为致密烧结体的质子导体BaZrO的(BZ)和掺y的BaZrO3(BZY)是通过加入NiO作为烧结促进剂,在1800℃-2000℃、5小时的短时间烧结得到的。而BZNY质子导体,则是由Ni、Y共掺杂的BaZrO3烧结得到的,并且烧结温度1300℃-1600℃。BZNY proton conductor: The proton conductor BaZrO (BZ) and y-doped BaZrO 3 (BZY) as a dense sintered body are obtained by adding NiO as a sintering accelerator and sintering at 1800°C-2000°C for a short time of 5 hours. The BZNY proton conductor is obtained by sintering BaZrO 3 co-doped with Ni and Y, and the sintering temperature is 1300°C-1600°C.

氢分离:主要适用于从含有氦、氩、氮、氕、氘、氚中至少两种成分的气体中提纯出氢及氢同位素的单组分纯气体。而在本示例性实施例中,尤其是针对核聚变环境中从含有低浓度氢气(含氢混合气体的氢气含量低于0.001%)的多组分混合气体中分离出纯氢气,即逆浓度梯度富集并提纯氢气。Hydrogen separation: It is mainly suitable for purifying single-component pure gas of hydrogen and hydrogen isotopes from gases containing at least two components of helium, argon, nitrogen, protium, deuterium and tritium. However, in this exemplary embodiment, it is especially aimed at separating pure hydrogen from a multi-component mixed gas containing low concentration hydrogen (the hydrogen content of the hydrogen-containing mixed gas is lower than 0.001%) in the nuclear fusion environment, that is, the reverse concentration gradient Enrich and purify hydrogen.

参见图1,图1示出了本发明一示例性实施例中提供的基于镍-BZNY质子导体的氢分离设备的结构示意图,包括:Referring to Fig. 1, Fig. 1 shows the structural representation of the hydrogen separation device based on nickel-BZNY proton conductor provided in an exemplary embodiment of the present invention, including:

BZNY质子导体1;BZNY Proton Conductor 1;

第一金属镍电极201和第二金属镍电极202,分别设置于BZNY质子导体1两侧;The first metal nickel electrode 201 and the second metal nickel electrode 202 are respectively arranged on both sides of the BZNY proton conductor 1;

第一引线301,导电端与第一金属镍电极201连接;第二引线302,导电端与第二金属镍电极202连接;第一引线301的接入端和第二引线302的接入端均与外部电信号输入设备4连接;The first lead 301, the conductive end is connected with the first metallic nickel electrode 201; the second lead 302, the conductive end is connected with the second metallic nickel electrode 202; the access end of the first lead 301 and the access end of the second lead 302 are both Connect with external electrical signal input device 4;

第一绝缘套筒501,连接在BZNY质子导体1位于第一金属镍电极201的一侧并套设在第一金属镍电极201的外围,第一绝缘套筒501内部形成氢气提取空间50101;The first insulating sleeve 501 is connected to the side of the BZNY proton conductor 1 located on the first metal nickel electrode 201 and is sleeved on the periphery of the first metal nickel electrode 201. A hydrogen extraction space 50101 is formed inside the first insulating sleeve 501;

第二绝缘套筒502,套设在第一绝缘套筒501外侧,与第一绝缘套筒501之间形成含氢混合气体提供空间50201。The second insulating sleeve 502 is sleeved on the outside of the first insulating sleeve 501 , and forms a hydrogen-containing mixed gas supply space 50201 between the first insulating sleeve 501 .

具体地,在本示例性实施例中,第二绝缘套筒502内的为含氢混合气体,第一绝缘套筒501内为纯氢气,包括BZNY质子导体1、第一金属镍电极201和第二金属镍电极202构成的质子导体膜片与第一绝缘套筒501为封闭式连接,从而对纯氢气和含氢混合气体进行隔断。在含氢混合气体提供空间50201中,含氢混合气体5内的氢同位素通过外部电信号输入设备4输出的电信号的控制下,通过BZNY质子导体1被抽取到装有纯氢气1的氢气提取空间50101。Specifically, in this exemplary embodiment, the second insulating sleeve 502 contains hydrogen-containing mixed gas, and the first insulating sleeve 501 contains pure hydrogen gas, including the BZNY proton conductor 1, the first metal nickel electrode 201 and the second The proton conductor diaphragm formed by the two metal nickel electrodes 202 is connected to the first insulating sleeve 501 in a closed manner, so as to isolate pure hydrogen gas and hydrogen-containing mixed gas. In the hydrogen-containing mixed gas supply space 50201, the hydrogen isotopes in the hydrogen-containing mixed gas 5 are extracted through the BZNY proton conductor 1 to the hydrogen extraction system containing pure hydrogen gas 1 under the control of the electrical signal output by the external electrical signal input device 4 Space 50101.

相较于现有技术,本申请具有以下优点:Compared with the prior art, the present application has the following advantages:

(1)在实际的使用研究过程中,当采用现有技术中的氧化物电极(NiO-NiO-BaZrxY1-xO3-δ或NiO-BaZrxCeyY1-x-yO3-δ作为阳极,LaxSr1-xCoyFe1-yO3-δ或LaxSr1-xMnO3-δ作为阴极)时,不仅氧化物电极则对氢的渗入具有一定的阻碍作用,而且氧化物电极在超低氢浓度(含氢混合气体的氢气含量低于0.001%)时分离氢需要约100V的电压。在此过高的氢分离电压下,不仅极大限制了其后续的工程化应用,而且会诱发了镍从BZNY中大量析出形成金属带,从而导致质子传导失效。(1) In the actual use research process, when using the oxide electrodes in the prior art (NiO-NiO-BaZr x Y 1-x O 3-δ or NiO-BaZr x Ce y Y 1-xy O 3- δ as the anode, La x Sr 1-x Co y Fe 1-y O 3-δ or La x Sr 1-x MnO 3-δ as the cathode), not only the oxide electrode has a certain hindering effect on the infiltration of hydrogen , and the oxide electrode needs a voltage of about 100V to separate hydrogen when the hydrogen concentration is ultra-low (the hydrogen content of the hydrogen-containing mixed gas is lower than 0.001%). Under this high hydrogen separation voltage, it not only greatly limits its subsequent engineering application, but also induces a large amount of nickel to be precipitated from BZNY to form metal bands, which leads to the failure of proton conduction.

而在本示例性实施例中,采用金属镍作为电极,因氢在镍中具有一定的溶解度,镍电极有利于超低浓度氢的渗入以完成后续的氢分离过程,且采用金属电极可以降低氢分离过程所需的给定电信号输入的工作电压。镍金属电极在超低浓度下工作所需的电压可小于10V且几乎不会诱发镍的析出现象。However, in this exemplary embodiment, metal nickel is used as the electrode. Because hydrogen has a certain solubility in nickel, the nickel electrode is conducive to the infiltration of ultra-low concentration hydrogen to complete the subsequent hydrogen separation process, and the use of metal electrodes can reduce the hydrogen concentration. The operating voltage for a given electrical signal input required for the separation process. The voltage required for the nickel metal electrode to work at an ultra-low concentration can be less than 10V and hardly induce the precipitation of nickel.

(2)在实际的使用研究过程中,当采用现有技术中的氧化物电极(NiO-NiO-BaZrxY1-xO3-δ或NiO-BaZrxCeyY1-x-yO3-δ作为阳极,LaxSr1-xCoyFe1-yO3-δ或LaxSr1-xMnO3-δ作为阴极)时,由于阴极材料、阳极材料不同,使得阴阳两级在实际加工工艺上,需要根据各自材料的烧结特性进行工艺与性能的权衡:若为了工艺,采用与质子导体实现稳固结合的烧结温度存在较大差异时,会导致氧化物电极和质子导体出现明显的界面弱结合问题,易发生膜层脱落现象;反之,则会使得加工工艺非常复杂。(2) In the actual use research process, when using the oxide electrodes in the prior art (NiO-NiO-BaZr x Y 1-x O 3-δ or NiO-BaZr x Ce y Y 1-xy O 3- δ as the anode, and La x Sr 1-x Co y Fe 1-y O 3-δ or La x Sr 1-x MnO 3-δ as the cathode), due to the different materials of the cathode and anode, the two stages of yin and yang are practically In terms of processing technology, it is necessary to balance the technology and performance according to the sintering characteristics of the respective materials: if there is a large difference in the sintering temperature for achieving a stable combination with the proton conductor for the sake of technology, it will lead to an obvious interface between the oxide electrode and the proton conductor The problem of weak bonding is prone to film peeling; otherwise, the processing technology will be very complicated.

在本示例性实施例中,呈现膜片中心对称结构,阴极和阳极采用同种材料,简化了膜片加工工艺,规避了现有技术中采用氧化物电极由于阴阳极材料不同、在实际加工工艺上需要根据各自材料的烧结特性进行工艺与性能权衡的困境。In this exemplary embodiment, the central symmetrical structure of the diaphragm is presented, and the same material is used for the cathode and the anode, which simplifies the diaphragm processing technology and avoids the fact that the oxide electrode used in the prior art is different in the actual processing technology due to the different materials of the cathode and anode. On the surface, it is necessary to make a trade-off between process and performance according to the sintering characteristics of the respective materials.

(3)在本示例性实施例中,采用BZNY材料作为质子导体,相比较于BZY(BaZrxY1- xO3-δ),镍元素的添加有利于质子导体的致密化和烧结温度的降低,进一步即降低能耗成本和对烧结炉设备的要求。BZY致密化需要近2000度的烧结温度,目前最高温度1600度的烧结炉与1800度的烧结炉的价格存在数量级差异。(3) In this exemplary embodiment, the BZNY material is used as the proton conductor. Compared with BZY (BaZr x Y 1- x O 3-δ ), the addition of nickel element is beneficial to the densification of the proton conductor and the improvement of the sintering temperature. Reduce, and further reduce energy consumption costs and requirements for sintering furnace equipment. The densification of BZY requires a sintering temperature of nearly 2000 degrees. At present, there is an order of magnitude difference in the price of a sintering furnace with a maximum temperature of 1600 degrees and a sintering furnace of 1800 degrees.

(4)在实际的使用研究过程中,当采用现有技术中的氧化物电极(NiO-NiO-BaZrxY1-xO3-δ或NiO-BaZrxCeyY1-x-yO3-δ作为阳极,LaxSr1-xCoyFe1-yO3-δ或LaxSr1-xMnO3-δ作为阴极)时,因氧化物电极采用涂敷技术,其界面结合力低,在实际工作几十个小时后易发生膜层分离和脱落现象。(4) In the actual use research process, when using the oxide electrodes in the prior art (NiO-NiO-BaZr x Y 1-x O 3-δ or NiO-BaZr x Ce y Y 1-xy O 3- δ as the anode, and La x Sr 1-x Co y Fe 1-y O 3-δ or La x Sr 1-x MnO 3-δ as the cathode), because the oxide electrode adopts coating technology, its interfacial binding force is low , after dozens of hours of actual work, the phenomenon of film layer separation and shedding is prone to occur.

(同时,可相比较于BZCY(BaZrxCeyY1-x-yO3-δ))在本示例性实施例中,BZNY质子导体1因成分中含有部分镍,与金属镍电极具有更好的兼容性和界面结合力,解决了氧化物电极膜易于从质子导体层脱落的难题。(At the same time, it can be compared with BZCY (BaZr x Ce y Y 1-xy O 3-δ )) In this exemplary embodiment, the BZNY proton conductor 1 has a better relationship with the metal nickel electrode due to the part of nickel contained in the composition. Compatibility and interface binding force solve the problem that the oxide electrode film is easy to fall off from the proton conductor layer.

下述内容将对各部件单独进行说明:Each part will be described separately as follows:

更优地,在一示例性实施例中,BZNY质子导体1作为氢分离过程中氢离子传递和运动的空间,具有特定组分结构和良好的工作性能。BZNY质子导体1包含但不限于厚度均匀的圆柱、长方体、正方体中心对称几何结构,具有BaZr0.8Ni0.04Y0.16O3-δ(BZNY)的特定组成。所述的BZNY质子导体1具有良好的质子电导率,可在500-800摄氏度中高温下保持良好稳定性,即后续的工作温度为500-800摄氏度。同时,BZNY质子导体1的最终烧结温度范围在1200-1600摄氏度。BZNY质子导体1的晶粒大小维持在毫米级或纳米级。More preferably, in an exemplary embodiment, the BZNY proton conductor 1 serves as a space for the transfer and movement of hydrogen ions during the hydrogen separation process, and has a specific component structure and good working performance. BZNY proton conductor 1 includes but not limited to cylinder, cuboid, and cube centrosymmetric geometric structures with uniform thickness, and has a specific composition of BaZr 0.8 Ni 0.04 Y 0.16 O 3-δ (BZNY). The BZNY proton conductor 1 has good proton conductivity and can maintain good stability at medium and high temperatures of 500-800 degrees Celsius, that is, the subsequent working temperature is 500-800 degrees Celsius. At the same time, the final sintering temperature range of BZNY proton conductor 1 is 1200-1600 degrees Celsius. The grain size of BZNY proton conductor 1 is maintained at the millimeter or nanometer level.

更优地,在一示例性实施例中,金属镍电极沉积或连接于所述BZNY质子导体1,且作为电信号输入的作用端。其中所述的金属镍电极制作的方法包含但不限于电镀法、溅射法、还原法、气相沉积法。所述第一金属镍电极201和第二金属镍电极202的厚度为10-1000nm,且金属镍电极微观结构致密且其晶粒呈现均匀分布特征,金属镍电极与BZNY质子导体1全部或局部连接紧密,宏观无明显分层。More preferably, in an exemplary embodiment, the metal nickel electrode is deposited or connected to the BZNY proton conductor 1, and serves as an input terminal for electrical signals. The methods for making metal nickel electrodes include but are not limited to electroplating, sputtering, reduction, and vapor deposition. The thickness of the first metal nickel electrode 201 and the second metal nickel electrode 202 is 10-1000nm, and the microstructure of the metal nickel electrode is dense and its crystal grains are evenly distributed, and the metal nickel electrode is fully or partially connected to the BZNY proton conductor 1 Tight, no obvious layering macroscopically.

其中,需要说明的是,当金属镍电极制作的方法采用的磁控溅射工艺时,相比氧化物电极采用的涂敷+烧结工艺,可以提升界面结合力,提高电极的膜层均匀性和工艺的成熟可靠性。因氧化物电极采用涂敷技术,其界面结合力低,在实际工作几十个小时后易发生膜层分离和脱落现象,而采用磁控溅射制备的金属镍电极在长达百小时的反复实验未发现电极和电解质的膜层分离和现象,且长时工作下的镍-BZNY质子导体1元件的氢分离性能未发现明显波动。Among them, it should be noted that when the magnetron sputtering process is used in the method of making the metal nickel electrode, compared with the coating + sintering process used in the oxide electrode, the interface bonding force can be improved, and the film layer uniformity of the electrode can be improved. The proven reliability of the process. Because the oxide electrode adopts coating technology, its interfacial bonding force is low, and the film layer separation and shedding are prone to occur after dozens of hours of actual work. The experiment did not find the membrane layer separation and phenomenon of the electrode and the electrolyte, and the hydrogen separation performance of the nickel-BZNY proton conductor 1 element under long-term work did not find obvious fluctuations.

更优地,在一示例性实施例中,外部电信号输入设备4输入以电压或电流形式的电信号作用于所述金属镍电极上。其中,电信号输入曲线涉及到的变电压大小范围在-10V至10V区间,恒电压大小范围在1-10V。可以通过对施加在元件两侧的电压或电流信号的追踪观察,表征和控制透氢量。More preferably, in an exemplary embodiment, the external electrical signal input device 4 inputs an electrical signal in the form of voltage or current to act on the metal nickel electrode. Wherein, the variable voltage involved in the electric signal input curve ranges from -10V to 10V, and the constant voltage ranges from 1-10V. The amount of hydrogen permeation can be characterized and controlled by tracking and observing the voltage or current signal applied to both sides of the element.

更优地,在一示例性实施例中,外部电信号输入设备4的电信号输入通过高纯度银线与所述的金属镍电极连接,即所述第一引线301和第二引线302均为高纯度银线,所述的高纯度银线的直径为0.2-0.6mm。更为具体地,第一引线301的导电端通过烧结、焊接、沉积、热压或冷压的方式与第一金属镍电极201连接,第二引线302的导电端通过烧结、焊接、沉积、热压或冷压的方式与第二金属镍电极202连接。电信号输入通过所述高纯度银线与金属镍电极连接的包含以点、线、面三种方式的直接或间接连接方式。More preferably, in an exemplary embodiment, the electrical signal input of the external electrical signal input device 4 is connected to the metal nickel electrode through a high-purity silver wire, that is, the first lead 301 and the second lead 302 are both High-purity silver wire, the diameter of the high-purity silver wire is 0.2-0.6mm. More specifically, the conductive end of the first lead 301 is connected to the first metal nickel electrode 201 by sintering, welding, deposition, hot pressing or cold pressing, and the conductive end of the second lead 302 is connected by sintering, welding, deposition, heat It is connected to the second metal nickel electrode 202 by pressing or cold pressing. The electrical signal input includes direct or indirect connection in three ways: point, line and surface through the high-purity silver wire and the metal nickel electrode.

其中,需要说明的是,采用镍金属电极,相比氧化物电极更适用使用银制引线实现连接,提高设备层面引线封装互连工艺的可靠性。Among them, it should be noted that the use of nickel metal electrodes is more suitable for connection with silver leads than oxide electrodes, which improves the reliability of the device-level lead packaging interconnection process.

多个所述的用于氢分离的镍-质子导体元件(BZNY质子导体1;以及第一金属镍电极201和第二金属镍电极202,分别设置于BZNY质子导体1两侧)级联可构成用于氢分离的系统,实现将氢同位素从核反应废气中分离回收以供循环使用的功能A plurality of nickel-proton conductor elements (BZNY proton conductor 1; and the first metal nickel electrode 201 and the second metal nickel electrode 202, respectively arranged on both sides of BZNY proton conductor 1) for hydrogen separation can be formed by cascading A system for hydrogen separation, which realizes the function of separating and recovering hydrogen isotopes from nuclear reaction waste gas for recycling

更优地,在一示例性实施例中,所述的第一绝缘套筒为耐高温陶瓷管,所述第二绝缘套筒为耐高温玻璃管。More preferably, in an exemplary embodiment, the first insulating sleeve is a high-temperature-resistant ceramic tube, and the second insulating sleeve is a high-temperature-resistant glass tube.

与上述示例性实施例具有相同的发明构思,本发明的又一示例性实施例提供所述的基于镍-BZNY质子导体的氢分离设备的使用方法,包括以下步骤:Having the same inventive concept as the above exemplary embodiment, another exemplary embodiment of the present invention provides a method for using the nickel-BZNY proton conductor-based hydrogen separation device, including the following steps:

将含氢混合气体通入第二绝缘套筒502;Pass the hydrogen-containing mixed gas into the second insulating sleeve 502;

第一金属镍电极201通过第一引线301接收外部电信号,同时第二金属镍电极202通过第二引线302接收外部信号;The first metal nickel electrode 201 receives an external electrical signal through the first lead wire 301, while the second metal nickel electrode 202 receives an external signal through the second lead wire 302;

含氢混合气体的氢同位素在电信号的控制下,通过BZNY质子导体1被抽取到第一绝缘套筒501的氢气提取空间50101。The hydrogen isotope of the hydrogen-containing mixed gas is extracted to the hydrogen extraction space 50101 of the first insulating sleeve 501 through the BZNY proton conductor 1 under the control of the electric signal.

下述内容将对多个部件的制备过程进行说明:The following will describe the preparation process of several parts:

BZNY质子导体1的组分为BaZr0.8Ni0.04Y0.16O3-δ,粉体合成使用自蔓延燃烧法,使用乙二胺四乙酸和柠檬酸作为助烧结剂,最终BZNY质子导体1的成片烧结温度为1350±5摄氏度,所得BZNY质子导体1保持稳定的相结构(如图2b),其电子扫描显微镜截面图显示晶粒致密且大小均匀,其晶粒大小直径为200-600nm(如图3b),BZNY质子导体1为直径在22±2mm的圆片(如图4),无明显弯曲现象,表面光滑无明显颗粒,其厚度在3-10mm范围内。The composition of BZNY proton conductor 1 is BaZr 0.8 Ni 0.04 Y 0.16 O 3-δ , the powder is synthesized using self-propagating combustion method, using ethylenediaminetetraacetic acid and citric acid as sintering aids, and the final sheet of BZNY proton conductor 1 The sintering temperature is 1350±5 degrees Celsius, and the obtained BZNY proton conductor 1 maintains a stable phase structure (as shown in Figure 2b). 3b), BZNY proton conductor 1 is a disc with a diameter of 22±2mm (as shown in Figure 4), without obvious bending phenomenon, smooth surface without obvious particles, and its thickness is in the range of 3-10mm.

双侧金属镍电极的制备方法选用的是射频磁控溅射镍技术,所用的射频磁控溅射镍靶为直径25mm,厚度6mm,镍纯度>99.99%的镍靶,使用的气氛为纯氩气,真空度在15-35mtorr范围内,溅射功率在30-180w范围内,预溅射在10-30mins范围内,生长溅射时间在5-20mins范围内,磁控溅射所得金属镍电极保持良好的金属镍相(如图2a),其厚度在500±150mm范围(如图3a),其形状为较标准的圆形,其直径在10-20mm(如图4中银白色部分),金属镍电极与BZNY质子导体1交界面无明显分层(如图3a)。The preparation method of the double-sided metal nickel electrode is radio frequency magnetron sputtering nickel technology. The radio frequency magnetron sputtering nickel target used is a nickel target with a diameter of 25mm, a thickness of 6mm, and a nickel purity >99.99%. The atmosphere used is pure argon Gas, the vacuum degree is in the range of 15-35mtorr, the sputtering power is in the range of 30-180w, the pre-sputtering is in the range of 10-30mins, the growth sputtering time is in the range of 5-20mins, and the metal nickel electrode obtained by magnetron sputtering Maintain a good metallic nickel phase (as shown in Figure 2a), its thickness is in the range of 500±150mm (as shown in Figure 3a), its shape is a relatively standard circle, its diameter is 10-20mm (as shown in the silvery white part in Figure 4), the metal There is no obvious delamination at the interface between the nickel electrode and the BZNY proton conductor 1 (as shown in Figure 3a).

图2为本发明提供的使用射频磁控溅射技术生长的金属镍电极(a)与BZNY质子导体1(b)的X射线衍射图,说明该工艺制备的镍电极和BZNY质子导体1的相结构单一,相纯度高。图3为本发明提供的射频磁控溅射金属镍电极截面(a)与BZNY质子导体1截面(b)的扫描电子显微镜图。说明镍电极与BZNY质子导体1的界面结合紧密,质子导体1的结晶度高。Fig. 2 is the X-ray diffraction pattern of the metal nickel electrode (a) and BZNY proton conductor 1 (b) grown by radio frequency magnetron sputtering technology provided by the present invention, illustrating the nickel electrode prepared by this process and the phase of BZNY proton conductor 1 Single structure, high phase purity. Fig. 3 is a scanning electron micrograph of the radio frequency magnetron sputtering metal nickel electrode section (a) and the BZNY proton conductor 1 section (b) provided by the present invention. It shows that the interface between the nickel electrode and the BZNY proton conductor 1 is closely combined, and the crystallinity of the proton conductor 1 is high.

银线连接处使用电达DAD-87导电银胶将BZNY质子导体1与直径为0.2mm的高纯度(纯度>99.99%)银线连接,连接采用烧结工艺,烧结温度为200±25摄氏度,连接方式为点连接,连接点6位于实施例中所制备元件的圆心处。Use DAD-87 conductive silver glue at the silver wire connection to connect the BZNY proton conductor 1 with a high-purity (purity>99.99%) silver wire with a diameter of 0.2mm. The method is point connection, and the connection point 6 is located at the center of the circle of the element prepared in the embodiment.

给定电信号输入直接作用于高纯度银线,间接作用于金属镍电极,其给定电信号输入的预设曲线为电压信号,设备为普塞斯S系列高精度台式数字源表,预设曲线输入电压范围为0-5V,步进电压为5mv,实际监测点数为1000点,检测所得数据包含电流、电压、功率、电阻等基本电学性能参数。其中,图5给出了从氢含量为0.001%的氢氦混合气体中提取氢气时,以电压形式提供的给定电信号输入与氢透过率之间的关系示意。The given electrical signal input acts directly on the high-purity silver wire and indirectly on the metal nickel electrode. The preset curve of the given electrical signal input is a voltage signal. The input voltage range of the curve is 0-5V, the step voltage is 5mv, and the actual monitoring points are 1000 points. The detected data includes basic electrical performance parameters such as current, voltage, power, and resistance. Among them, Fig. 5 shows the relationship between the given electrical signal input in the form of voltage and the hydrogen transmission rate when hydrogen is extracted from the hydrogen-helium mixed gas with a hydrogen content of 0.001%.

显然,上述实施例仅仅是为清楚地说明所作的举例,而并非对实施方式的限定,对于所属领域的普通技术人员来说,在上述说明的基础上还可以做出其他不同形式的变化或变动。这里无需也无法对所有的实施方式予以穷举。而由此所引申出的显而易见的变化或变动仍处于本发明创造的保护范围之中。Apparently, the above-mentioned embodiment is only an example for clearly explaining, rather than limiting the implementation. For those of ordinary skill in the art, other changes or changes in different forms can be made on the basis of the above-mentioned description. . It is not necessary and impossible to exhaustively list all the implementation manners here. However, the obvious changes or changes derived therefrom are still within the scope of protection of the present invention.

Claims (10)

1. A hydrogen separation apparatus based on a nickel-BZNY proton conductor, characterized in that: the method comprises the following steps:
a BZNY proton conductor;
the first metal nickel electrode and the second metal nickel electrode are respectively arranged on two sides of the BZNY proton conductor;
the conductive end of the first lead is connected with the first metal nickel electrode; the conductive end of the second lead is connected with the second metal nickel electrode; the access end of the first lead and the access end of the second lead are both connected with external electric signal input equipment;
the first insulating sleeve is connected to one side, located on the first metal nickel electrode, of the BZNY proton conductor and sleeved on the periphery of the first metal nickel electrode, and a hydrogen extraction space is formed inside the first insulating sleeve;
the second insulating sleeve is sleeved outside the first insulating sleeve, and a hydrogen-containing mixed gas providing space is formed between the second insulating sleeve and the first insulating sleeve.
2. A nickel-BZNY proton conductor based hydrogen separation apparatus as claimed in claim 1, wherein: the conductive end of the first lead is connected with the first metal nickel electrode in a sintering, welding, depositing, hot pressing or cold pressing mode, and the conductive end of the second lead is connected with the second metal nickel electrode in a sintering, welding, depositing, hot pressing or cold pressing mode.
3. A nickel-BZNY proton conductor based hydrogen separation apparatus as claimed in claim 1, wherein: the first insulating sleeve is a high-temperature-resistant ceramic tube, and the second insulating sleeve is a high-temperature-resistant glass tube.
4. A nickel-BZNY proton conductor-based hydrogen separation apparatus as claimed in claim 1, wherein: the hydrogen content of the hydrogen-containing mixed gas is less than 0.001%.
5. A nickel-BZNY proton conductor-based hydrogen separation apparatus as claimed in claim 1, wherein: the variable voltage range of the input curve of the electric signal input by the external electric signal input equipment is between-10V and 10V, and the constant voltage range is between 1V and 10V.
6. A nickel-BZNY proton conductor-based hydrogen separation apparatus as claimed in claim 1, wherein: the final sintering temperature range of the BZNY proton conductor is 1200-1600 ℃.
7. A nickel-BZNY proton conductor-based hydrogen separation apparatus as claimed in claim 1 or 2, wherein: the first lead and the second lead are both high-purity silver wires.
8. A nickel-BZNY proton conductor-based hydrogen separation apparatus as claimed in claim 1, wherein: the method for manufacturing the metal nickel electrode comprises an electroplating method, a sputtering method, a reduction method and a vapor deposition method.
9. A nickel-BZNY proton conductor-based hydrogen separation apparatus as claimed in claim 1, wherein: the thickness of the first metal nickel electrode and the second metal nickel electrode is 10-1000nm, and the diameter of the first lead and the diameter of the second lead are 0.2-0.6mm.
10. A method of using a nickel-BZNY proton conductor based hydrogen separation apparatus as claimed in any one of claims 1 to 9, wherein: the method comprises the following steps:
introducing a hydrogen-containing mixed gas into the second insulating sleeve;
the first metal nickel electrode receives an external electric signal through a first lead, and the second metal nickel electrode receives an external signal through a second lead;
the hydrogen isotope of the hydrogen-containing mixed gas is extracted to the hydrogen extraction space of the first insulating sleeve through the BZNY proton conductor under the control of an electric signal.
CN202211400552.2A 2022-11-09 2022-11-09 Hydrogen separation apparatus based on nickel-BZNY proton conductor and method of use Active CN115646191B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202211400552.2A CN115646191B (en) 2022-11-09 2022-11-09 Hydrogen separation apparatus based on nickel-BZNY proton conductor and method of use

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202211400552.2A CN115646191B (en) 2022-11-09 2022-11-09 Hydrogen separation apparatus based on nickel-BZNY proton conductor and method of use

Publications (2)

Publication Number Publication Date
CN115646191A true CN115646191A (en) 2023-01-31
CN115646191B CN115646191B (en) 2024-10-01

Family

ID=85016863

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202211400552.2A Active CN115646191B (en) 2022-11-09 2022-11-09 Hydrogen separation apparatus based on nickel-BZNY proton conductor and method of use

Country Status (1)

Country Link
CN (1) CN115646191B (en)

Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5393325A (en) * 1990-08-10 1995-02-28 Bend Research, Inc. Composite hydrogen separation metal membrane
US5645626A (en) * 1990-08-10 1997-07-08 Bend Research, Inc. Composite hydrogen separation element and module
US5932361A (en) * 1996-10-21 1999-08-03 Belyakov; Vladimir Nikolaevich Ceramic based membranes
JP2004311159A (en) * 2003-04-04 2004-11-04 Central Res Inst Of Electric Power Ind High pressure hydrogen production method and apparatus and fuel cell vehicle
US20090104500A1 (en) * 2004-12-23 2009-04-23 Universitetet I Oslo Proton Conductors
GB201309336D0 (en) * 2013-05-23 2013-07-10 Protia As Proton conducing ceramic membrage
US20150314232A1 (en) * 2014-04-03 2015-11-05 University Of South Carolina Novel Chemically Stable Ceramic-Metal Composite Membrane for Hydrogen Separation
CN107354479A (en) * 2017-07-26 2017-11-17 合肥工业大学 A kind of anode preparation method suitable for high-temperature electrochemistry hydrogen pump
CN109289554A (en) * 2018-11-07 2019-02-01 山东理工大学 Proton-electron mixed conductor hydrogen permeable membrane and preparation method thereof, and hydrogen permeation membrane reactor
CN109563634A (en) * 2016-08-09 2019-04-02 本田技研工业株式会社 Hydrogen processing unit
CN110627019A (en) * 2019-09-26 2019-12-31 电子科技大学 A hydrogen isotope extraction component under high temperature conditions of hydrogen-containing mixed gas
CN111418027A (en) * 2017-11-29 2020-07-14 国立大学法人京都大学 Proton conductor, proton-conducting cell structure, water vapor electrolytic cell, and method for producing hydrogen electrode-solid electrolyte layer composite
CN111689777A (en) * 2020-06-18 2020-09-22 苏州溢亮材料科技有限公司 Symmetric ceramic hydrogen pump capable of realizing hydrogen purification in complex scene and preparation method thereof
CN212770985U (en) * 2020-08-25 2021-03-23 李连洪 Hydrogen production assembly and hydrogen production machine

Patent Citations (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5645626A (en) * 1990-08-10 1997-07-08 Bend Research, Inc. Composite hydrogen separation element and module
US5393325A (en) * 1990-08-10 1995-02-28 Bend Research, Inc. Composite hydrogen separation metal membrane
US5932361A (en) * 1996-10-21 1999-08-03 Belyakov; Vladimir Nikolaevich Ceramic based membranes
JP2004311159A (en) * 2003-04-04 2004-11-04 Central Res Inst Of Electric Power Ind High pressure hydrogen production method and apparatus and fuel cell vehicle
US20090104500A1 (en) * 2004-12-23 2009-04-23 Universitetet I Oslo Proton Conductors
US20160096151A1 (en) * 2013-05-23 2016-04-07 Protia As Proton conducting ceramic membrane
GB201309336D0 (en) * 2013-05-23 2013-07-10 Protia As Proton conducing ceramic membrage
US20150314232A1 (en) * 2014-04-03 2015-11-05 University Of South Carolina Novel Chemically Stable Ceramic-Metal Composite Membrane for Hydrogen Separation
CN109563634A (en) * 2016-08-09 2019-04-02 本田技研工业株式会社 Hydrogen processing unit
CN107354479A (en) * 2017-07-26 2017-11-17 合肥工业大学 A kind of anode preparation method suitable for high-temperature electrochemistry hydrogen pump
CN111418027A (en) * 2017-11-29 2020-07-14 国立大学法人京都大学 Proton conductor, proton-conducting cell structure, water vapor electrolytic cell, and method for producing hydrogen electrode-solid electrolyte layer composite
CN109289554A (en) * 2018-11-07 2019-02-01 山东理工大学 Proton-electron mixed conductor hydrogen permeable membrane and preparation method thereof, and hydrogen permeation membrane reactor
CN110627019A (en) * 2019-09-26 2019-12-31 电子科技大学 A hydrogen isotope extraction component under high temperature conditions of hydrogen-containing mixed gas
CN111689777A (en) * 2020-06-18 2020-09-22 苏州溢亮材料科技有限公司 Symmetric ceramic hydrogen pump capable of realizing hydrogen purification in complex scene and preparation method thereof
CN212770985U (en) * 2020-08-25 2021-03-23 李连洪 Hydrogen production assembly and hydrogen production machine

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
FANG, SM (FANG, SHUMIN): "Relationship between fabrication method and chemical stability of Ni-BaZr0.8Y0.2O3-δ membrane", 《 JOURNAL OF POWER SOURCES》, vol. 278, 15 March 2015 (2015-03-15), pages 614 - 622 *
朱志文: "高性能与高稳定性致密陶瓷氢分离膜研究", 《CNKI博士学位论文全文库》, no. 10, 15 October 2013 (2013-10-15), pages 1 - 119 *

Also Published As

Publication number Publication date
CN115646191B (en) 2024-10-01

Similar Documents

Publication Publication Date Title
US6887361B1 (en) Method for making thin-film ceramic membrane on non-shrinking continuous or porous substrates by electrophoretic deposition
JPH05502060A (en) Ceramic solid electrolyte based electrochemical oxygen concentrator
Li et al. Enhanced reliability of Ni-Fe alloys supported SOFCs with ex-Situ sintered La0. 8Sr0. 2MnO3− δ Coated Ba0. 5Sr0. 5Co0. 8Fe0. 2O3–δ Cathode
Yang et al. Novel high-entropy BaCo0. 2Zn0. 2Ga0. 2Zr0. 2Y0. 2O3-δ cathode for proton ceramic fuel cells
JP6600300B2 (en) Multi-layer arrangement for solid electrolyte
CN101260547B (en) Method for directly preparing AB5 type hydrogen storage alloy from metal oxide mixture
CN115646191A (en) Hydrogen separation device and method of use based on nickel-BZNY proton conductor
Zhang et al. Intermediate temperature solid oxide cell with a barrier layer free oxygen electrode and phase inversion derived hydrogen electrode
JP3411064B2 (en) Method for producing solid electrolyte sintered body for solid oxide fuel cell
KR101100349B1 (en) Solid electrolyte fuel cell manufacturing method and solid oxide fuel cell manufacturing method using same
CN115332619A (en) High-entropy oxide solid electrolyte material for solid battery and preparation method and application thereof
KR101054005B1 (en) Stainless steel metal connectors with phase stability and electrical conductivity coated with NOO conductive oxide
KR101390733B1 (en) Preparing method of ni/ysz core-shell composite for sofc
Macalisang et al. Screen-Printing of NiO-ScSZ on YSZ Substrate Using Solid-State Reaction and Glycine-Nitrate Process Precursors for Solid Oxide Electrochemical Cells
Markin et al. High temperature solid electrolyte fuel cells
CN100534950C (en) Method for producing LaGaO* group solid electrolyte target material
JPH1021930A (en) Fuel electrode of solid oxide fuel cell
Zhuang et al. High-performance novel anode-supported microtubular protonic ceramic fuel cells via highly efficient and simplified extrusion technology
CN111180772B (en) Preparation method for preparing solid oxide fuel cell material
JP7535981B2 (en) Oxide-based solid electrolytes and all-solid-state lithium-ion batteries
CN113955814B (en) NiCl synthesized at low temperature 2 Powder and application
Susanto et al. Study on the composite structure of cobalt-free oxides as cathodes for intermediate temperature solid oxide fuel cells (IT-SOFCs)
Wang et al. Mechanism Analysis of the Reduction Process of the NiO-YSZ Anode of a Solid Oxide Fuel Cell by Hydrogen
CN108828045A (en) A kind of zirconic acid calcium material, the preparation method and its usage of doping metals
Zhang et al. Investigation of plasma sprayed Sr0· 7La0· 3TiO3/La0· 2Sr0· 8MnO3 Bi-layer interconnector performance and its application in high power tubular solid oxide fuel cells

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20240612

Address after: Room 351, Building 1, the Taihu Lake Laboratory, No. 1040, Zhongxing Avenue, Balidian Town, Wuxing District, Huzhou City, Zhejiang Province, 313000

Applicant after: Lingtian Technology (Huzhou) Co.,Ltd.

Country or region after: China

Address before: 611731, No. 2006, West Avenue, Chengdu hi tech Zone (West District, Sichuan)

Applicant before: University of Electronic Science and Technology of China

Country or region before: China

GR01 Patent grant
GR01 Patent grant