CN118374814A - A device for preparing arsine by double-anode electrocatalysis and its application - Google Patents
A device for preparing arsine by double-anode electrocatalysis and its application Download PDFInfo
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Abstract
本申请公开了一种双阳极电催化制备砷烷的装置及应用,本申请装置包括阴极电解槽及设置于阴极电解槽两侧的两个阳极电解槽,阴极电解槽与阳极电解槽之间分别用隔膜隔开,隔膜面向阳极电解槽的一侧面上紧密贴合有阳极催化剂;阴极电解槽内部穿插有阴极电极,且阴极电极与电源负极通过导线连接,两个隔膜相反两侧的两个阳极催化剂通过导线并联与电源正极连接。本发明通过设计“双通道”阳极电解槽结构,通过增加阳极电解槽及阳极催化剂的数量调控反应转移质子的能力,直接提高了反应的电流密度,一方面提高了阳极产生氧气的速率,另一方面加速了阴极砷烷的产生。
The present application discloses a device and application for preparing arsine by dual anode electrocatalysis. The device of the present application comprises a cathode electrolyzer and two anode electrolyzers arranged on both sides of the cathode electrolyzer. The cathode electrolyzer and the anode electrolyzer are separated by a diaphragm, and an anode catalyst is tightly fitted on one side of the diaphragm facing the anode electrolyzer; a cathode electrode is inserted into the cathode electrolyzer, and the cathode electrode is connected to the negative electrode of the power supply through a wire, and two anode catalysts on opposite sides of the two diaphragms are connected to the positive electrode of the power supply in parallel through a wire. The present invention directly improves the current density of the reaction by designing a "dual-channel" anode electrolyzer structure and regulating the ability of the reaction to transfer protons by increasing the number of anode electrolyzers and anode catalysts, thereby increasing the rate of oxygen generation at the anode on the one hand and accelerating the generation of arsine at the cathode on the other hand.
Description
技术领域Technical Field
本发明属于电催化技术领域,具体涉及一种双阳极电催化制备砷烷的装置及应用。The invention belongs to the technical field of electrocatalysis, and in particular relates to a device for preparing arsine by double-anode electrocatalysis and its application.
背景技术Background technique
随着科技的不断进步,半导体芯片和液晶面板产业的发展占据了重要地位,对于电子化学品的需求也逐年提升,半导体芯片和液晶面板的生产涉及了近三百种电子化学品,然而电子化学品的发展却不容乐观。由于电子化学品生产过程条件的苛刻,生产过程存在非常大的安全隐患,导致了其生产过程成本巨大,严重影响了其生产过程。With the continuous advancement of science and technology, the development of semiconductor chips and liquid crystal panel industries has occupied an important position, and the demand for electronic chemicals has also increased year by year. The production of semiconductor chips and liquid crystal panels involves nearly 300 kinds of electronic chemicals, but the development of electronic chemicals is not optimistic. Due to the harsh conditions of the production process of electronic chemicals, there are very large safety hazards in the production process, which leads to huge production costs and seriously affects its production process.
电子特气作为一种常见的电子化学品,广泛应用于成膜过程、干式刻蚀、化学清洗等方面,尤其是在集成电路,平面显示器件和半导体方面是一种不可或缺的材料。目前制备砷烷的方式主要依靠热化学方式,通过砷化合物的形成,进一步通过与酸反应形成砷烷,但是在该过程中,由于气体不纯导致的成本高,过程繁琐,反应过程具有爆炸的危险的安全隐患等。然而电催化制备砷烷以其独特的优势吸引了众多研究者的关注,电催化过程通过电流和催化剂可以对反应进行精准的调控,实现砷烷的可控制备。但是,对于电催化反应器的研究还是比较少,高效、安全的电反应器的发展成为一种亟需。As a common electronic chemical, electronic special gases are widely used in film forming processes, dry etching, chemical cleaning, etc., especially in integrated circuits, flat panel display devices and semiconductors. It is an indispensable material. At present, the preparation method of arsine mainly relies on thermochemical methods, through the formation of arsenic compounds, and further through the reaction with acid to form arsine. However, in this process, the cost is high due to the impure gas, the process is cumbersome, and the reaction process has the safety hazard of explosion. However, the electrocatalytic preparation of arsine has attracted the attention of many researchers with its unique advantages. The electrocatalytic process can accurately control the reaction through electric current and catalysts to achieve controllable preparation of arsine. However, there is still relatively little research on electrocatalytic reactors, and the development of efficient and safe electroreactors has become an urgent need.
发明内容Summary of the invention
鉴于现有技术存在的问题,本发明的目的在于提供一种双阳极电催化制备砷烷的装置,通过设计双阳极电解槽,实现双通道离子的快速传输,提高催化反应的速率,进而提升砷烷的产量。阳极电解槽与阴极电解槽之间通过隔膜进行分离,实现氧化性气体和强还原性气体砷烷的绝对分离,形成安全化砷烷的制备。该反应器与以往设备相比,设备简单,反应速率快,提高了产物的产量。In view of the problems existing in the prior art, the purpose of the present invention is to provide a device for preparing arsine by dual-anode electrocatalysis. By designing a dual-anode electrolyzer, rapid transmission of dual-channel ions is achieved, the rate of catalytic reaction is increased, and the yield of arsine is increased. The anode electrolyzer and the cathode electrolyzer are separated by a diaphragm to achieve absolute separation of oxidizing gas and strongly reducing gas arsine, thereby forming a safe preparation of arsine. Compared with previous equipment, the reactor is simple in equipment, fast in reaction rate, and increases the yield of the product.
所述的一种双阳极电催化制备砷烷的装置,包括阴极电解槽以及设置于阴极电解槽左右两侧的两个阳极电解槽,阴极电解槽与其两侧的两个阳极电解槽之间分别用隔膜隔开,通过隔膜实现离子的快速传输,隔膜面向阳极电解槽的一侧面上紧密贴合有阳极催化剂;阳极电解槽的底部和顶部分别设有阳极进液口和阳极排液排气口,阴极电解槽的底部和顶部分别设有阴极进液口和阴极排液排气口,阴极电解槽内部穿插有阴极电极,且阴极电极与电源负极通过导线连接,两个隔膜相反两侧的两个阳极催化剂通过导线并联与电源正极连接。电解生成的氧气从阳极排液排气口排出,砷烷从阴极排液排气口排出。阴极电解槽中设置有阴极电极,阴极电极选用砷单质材料。The device for preparing arsine by dual-anode electrocatalysis comprises a cathode electrolyzer and two anode electrolyzers arranged on the left and right sides of the cathode electrolyzer, wherein the cathode electrolyzer and the two anode electrolyzers on both sides thereof are separated by diaphragms, and the rapid transmission of ions is achieved through the diaphragms, and an anode catalyst is tightly fitted on one side of the diaphragm facing the anode electrolyzer; the bottom and top of the anode electrolyzer are respectively provided with an anode liquid inlet and an anode liquid discharge and exhaust port, and the bottom and top of the cathode electrolyzer are respectively provided with a cathode liquid inlet and a cathode liquid discharge and exhaust port, and a cathode electrode is inserted into the cathode electrolyzer, and the cathode electrode is connected to the negative pole of the power supply through a wire, and two anode catalysts on opposite sides of the two diaphragms are connected in parallel with the positive pole of the power supply through a wire. Oxygen generated by electrolysis is discharged from the anode liquid discharge and exhaust port, and arsine is discharged from the cathode liquid discharge and exhaust port. A cathode electrode is provided in the cathode electrolyzer, and the cathode electrode is made of arsenic single substance material.
进一步地,本发明还限定了阳极电解槽和阴极电解槽采用有机材料,如PTFE、PE和PVC等,优选PE。Furthermore, the present invention also stipulates that the anode electrolytic cell and the cathode electrolytic cell are made of organic materials, such as PTFE, PE and PVC, etc., preferably PE.
进一步地,本发明还限定了阳极槽和阴极槽两者之间存在隔膜,隔膜采用陶瓷膜、阴离子膜和质子膜,优先选用Nafion 115(质子膜)。Furthermore, the present invention also defines that there is a diaphragm between the anode tank and the cathode tank, and the diaphragm is a ceramic membrane, an anion membrane or a proton membrane, and Nafion 115 (proton membrane) is preferably used.
进一步地,本发明还限定了阳极电解槽有一组(两个),分别位于阴极电解槽的左右两侧且平行设置,阴极电解槽与隔膜的交接处之间以及隔膜与阳极电解槽的交接处之间,均使用垫片进行密封。Furthermore, the present invention also defines that there is a group (two) of anode electrolytic cells, which are respectively located on the left and right sides of the cathode electrolytic cell and are arranged in parallel, and gaskets are used to seal the junction between the cathode electrolytic cell and the diaphragm, and the junction between the diaphragm and the anode electrolytic cell.
进一步地,本发明还限定了阴极电解槽的侧部中部设有一个圆形的口,为阴极电极口,阴极电极从阴极电极口横向插入在所述阴极电解槽内,且阴极电极与阴极电极口的交接处设有密封装置,阴极电极选用砷单质材料,阴极电极为圆棒结构。Furthermore, the present invention also defines that a circular opening is provided in the middle of the side of the cathode electrolytic cell, which is the cathode electrode opening. The cathode electrode is laterally inserted into the cathode electrolytic cell from the cathode electrode opening, and a sealing device is provided at the junction of the cathode electrode and the cathode electrode opening. The cathode electrode is made of arsenic single-element material and has a round rod structure.
本发明还提供了所述一种双阳极电催化制备砷烷的装置的应用,应用过程如下:阴极电解槽及两个阳极电解槽内分别通入电解液,电解液采用0.5-3M的KOH水溶液,通电下进行电解反应,反应的电流为400-600mA,阴极产物砷烷气体从阴极电解槽的阴极排液排气口排出进行收集。The present invention also provides an application of the dual-anode electrocatalytic preparation of arsine device, and the application process is as follows: electrolytes are respectively introduced into the cathode electrolytic cell and the two anode electrolytic cells, the electrolyte adopts a 0.5-3M KOH aqueous solution, and an electrolytic reaction is carried out under power, the reaction current is 400-600mA, and the cathode product arsine gas is discharged from the cathode liquid exhaust port of the cathode electrolytic cell for collection.
进一步地,阳极催化剂为具有铱镀层的钛阳极,以钛片为电极基底,铱镀层为二氧化铱,铱镀层在电极基底上的负载量为0.2-2mg/cm2;电解反应时阳极产物为氧气,氧气从阳极电解槽顶部的阳极排液排气口排出进行收集。Furthermore, the anode catalyst is a titanium anode with an iridium coating, with a titanium sheet as the electrode substrate, the iridium coating is iridium dioxide, and the loading amount of the iridium coating on the electrode substrate is 0.2-2 mg/ cm2 ; the anode product during the electrolysis reaction is oxygen, which is discharged from the anode liquid exhaust port at the top of the anode electrolyzer for collection.
进一步地,本发明还限定了本发明中所有的密封垫可采用聚四氟乙烯垫片、膨体四氟垫片等,优选膨体四氟垫片。Furthermore, the present invention also defines that all the sealing gaskets in the present invention can be polytetrafluoroethylene gaskets, expanded polytetrafluoroethylene gaskets, etc., preferably expanded polytetrafluoroethylene gaskets.
与现有技术相比较,本发明的有益效果:Compared with the prior art, the present invention has the following beneficial effects:
1)本发明通过设计“双通道”阳极电解槽结构,实现质子的快速传输,一方面提高了阳极产生氧气的速率,另一方面加速了阴极砷烷的产生。本发明的设计,实现了高产量砷烷的制备,提高了质子的利用效率。1) The present invention realizes the rapid transmission of protons by designing a "dual-channel" anode electrolyzer structure, which improves the rate of oxygen generation at the anode and accelerates the generation of arsine at the cathode. The design of the present invention realizes the preparation of arsine with high yield and improves the utilization efficiency of protons.
2)本发明通过将阳极催化剂紧贴于隔膜上,提高了阳极反应后形成的H+的传输,缩短了电极与膜之间距离,减少了反应阻力,有效提高了催化剂材料的稳定性,同时避免因过高的电阻发热导致的催化效率降低。2) The present invention improves the transmission of H + formed after the anode reaction by placing the anode catalyst in close contact with the diaphragm, shortens the distance between the electrode and the membrane, reduces the reaction resistance, effectively improves the stability of the catalyst material, and avoids the reduction of catalytic efficiency due to excessive resistance heating.
3)本发明的一种双阳极电催化制备砷烷的装置,通过增加阳极电解槽及阳极催化剂的数量调控反应转移质子的能力,直接提高了反应的电流密度,间接的增加了阴极通过还原生成的As3-与H+的结合几率,提高了反应的传质能力,进而实现了砷烷产量的提高。本发明的装置构造简单,成本低,效率高,具有很大的应用潜力。3) The dual-anode electrocatalytic preparation of arsine device of the present invention regulates the ability of the reaction to transfer protons by increasing the number of anode electrolytic cells and anode catalysts, directly increases the current density of the reaction, indirectly increases the probability of the As 3- generated by reduction at the cathode and H + combining, improves the mass transfer capacity of the reaction, and thus achieves an increase in the yield of arsine. The device of the present invention has a simple structure, low cost, high efficiency, and great application potential.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1为本发明一种双阳极电催化制备砷烷的装置的整体结构示意图;FIG1 is a schematic diagram of the overall structure of a device for preparing arsine by dual-anode electrocatalysis according to the present invention;
图2为本发明的阴极电解槽结构示意图。FIG. 2 is a schematic diagram of the structure of the cathode electrolytic cell of the present invention.
图3为本发明对比例的整体结构示意图。FIG. 3 is a schematic diagram of the overall structure of a comparative example of the present invention.
图1中:1.阳极电解槽;2.阴极电解槽;3.阳极电极;4.阳极催化剂;5.质子交换膜;6.阴极电极;7.直流电源正极;8.直流电源负极;9.阳极出液口;10.阳极进液口。In Figure 1: 1. anode electrolytic cell; 2. cathode electrolytic cell; 3. anode electrode; 4. anode catalyst; 5. proton exchange membrane; 6. cathode electrode; 7. positive electrode of DC power supply; 8. negative electrode of DC power supply; 9. anode liquid outlet; 10. anode liquid inlet.
图2中:11.阴极出液口;12.阴极进液口。In Figure 2: 11. cathode liquid outlet; 12. cathode liquid inlet.
具体实施方式Detailed ways
下面结合具体实施例对本发明作进一步说明,但本发明的保护范围并不限于此。The present invention will be further described below in conjunction with specific embodiments, but the protection scope of the present invention is not limited thereto.
如图1所示,本发明的一种双阳极电催化制备砷烷的装置,该设备包括阴极电解槽2以及设置于阴极电解槽2左右两侧的两个阳极电解槽1,阴极电解槽2与其两侧的两个阳极电解槽1之间分别用隔膜5隔开,通过隔膜5实现离子的快速传输,为了防止阴极电解槽2和阳极电解槽1不经过隔膜5直接相通和漏液,在隔膜5两侧设有垫片,起到密封的作用。也就是说,阴极电解槽2与隔膜5的交接处之间以及隔膜5与阳极电解槽1的交接处之间,均使用垫片进行密封。As shown in FIG1 , a device for preparing arsine by dual-anode electrocatalysis of the present invention comprises a cathode electrolytic cell 2 and two anode electrolytic cells 1 arranged on the left and right sides of the cathode electrolytic cell 2. The cathode electrolytic cell 2 and the two anode electrolytic cells 1 on both sides thereof are separated by diaphragms 5, respectively, and the rapid transmission of ions is achieved through the diaphragms 5. In order to prevent the cathode electrolytic cell 2 and the anode electrolytic cell 1 from being directly connected and leaking without passing through the diaphragm 5, gaskets are arranged on both sides of the diaphragm 5 to play a sealing role. That is to say, the junction between the cathode electrolytic cell 2 and the diaphragm 5 and the junction between the diaphragm 5 and the anode electrolytic cell 1 are both sealed with gaskets.
阳极电解槽1的顶部设有阳极排液排气口9,使用外牙聚四氟乙烯转接头与阳极产物收集器相连,底部设有阳极进液口10,同样用外牙聚四氟乙烯转接头与进料罐相连,每一个阳极电解槽1均内设有阳极催化剂电极3,并且与隔膜5紧密贴合。两个阳极电解槽1中,两个隔膜5相反两侧的两个阳极催化剂4通过导线并联与电源正极7连接,生成的氧气从阳极排液排气口9排出。The top of the anode electrolyzer 1 is provided with an anode liquid discharge vent 9, which is connected to the anode product collector using an external polytetrafluoroethylene adapter, and the bottom is provided with an anode liquid inlet 10, which is also connected to the feed tank using an external polytetrafluoroethylene adapter. Each anode electrolyzer 1 is provided with an anode catalyst electrode 3, which is tightly fitted with the diaphragm 5. In the two anode electrolyzers 1, the two anode catalysts 4 on the opposite sides of the two diaphragms 5 are connected in parallel to the positive electrode 7 of the power supply through a wire, and the generated oxygen is discharged from the anode liquid discharge vent 9.
如图2所示,本发明的阴极电解槽的顶部设有阴极排液排气口11,使用外牙聚四氟乙烯转接头与阴极产物收集器相连,底部设有阴极进液口12,同样用外牙聚四氟乙烯转接头与进料罐相连。位于阴极电解槽的侧部中部设有一个圆形的口,为阴极电极口6。阴极电极从阴极电极口6横向插入在所述阴极电解槽2内,阴极电极与阴极电极口6的交接处设有密封垫,阴极电极与电源负极8通过导线连接,产物砷烷从阴极排液排气口11排出。As shown in FIG2 , the cathode electrolyzer of the present invention is provided with a cathode liquid discharge and exhaust port 11 at the top, which is connected to the cathode product collector using an external polytetrafluoroethylene adapter, and a cathode liquid inlet 12 is provided at the bottom, which is also connected to the feed tank using an external polytetrafluoroethylene adapter. A circular opening is provided in the middle of the side of the cathode electrolyzer, which is the cathode electrode opening 6. The cathode electrode is laterally inserted into the cathode electrolyzer 2 from the cathode electrode opening 6, and a sealing gasket is provided at the junction of the cathode electrode and the cathode electrode opening 6. The cathode electrode is connected to the negative electrode 8 of the power supply through a wire, and the product arsine is discharged from the cathode liquid discharge and exhaust port 11.
为了进一步说明,本发明的进一步地,本发明的阳极电解槽1和阴极电解槽2采用有机材料,如PTFE、PE和PVC等,优选PE。阳极电解槽1和阴极电解槽2两者之间存在隔膜5,隔膜采用陶瓷膜、阴离子膜和质子膜等,优先选用Nafion 115(质子膜)。阳极催化剂4可选用铂镀层的钛或镍、铱镀层的钛或镍等,优选铱镀层的钛。电源与电极之间的连接处采用铜、铝及其合金材料,优选铜,并通过烫锡进行处理。所有的密封垫可采用聚四氟乙烯垫片、膨体四氟垫片,优选膨体四氟垫片。To further illustrate, further in the present invention, the anode electrolyzer 1 and the cathode electrolyzer 2 of the present invention are made of organic materials, such as PTFE, PE and PVC, etc., preferably PE. There is a diaphragm 5 between the anode electrolyzer 1 and the cathode electrolyzer 2, and the diaphragm is made of ceramic membrane, anion membrane and proton membrane, etc., preferably Nafion 115 (proton membrane). The anode catalyst 4 can be made of platinum-plated titanium or nickel, iridium-plated titanium or nickel, etc., preferably iridium-plated titanium. The connection between the power supply and the electrode is made of copper, aluminum and their alloy materials, preferably copper, and is treated by hot tinning. All sealing gaskets can be made of polytetrafluoroethylene gaskets, expanded polytetrafluoroethylene gaskets, preferably expanded polytetrafluoroethylene gaskets.
实施例1:一种双阳极电催化制备砷烷的装置Example 1: A dual-anode electrocatalytic device for preparing arsenic
装置结构参见图1-2,阴极电解槽位于两个阳极电解槽之间,与阳极电解槽之间设有Nafion 115膜,选择性的透过反应过程中的离子,同时具有分离阴阳极电解槽产物的作用,达到爆炸气体的绝对分离,实现安全化砷烷生产。在Nafion 115膜面向阳极电解槽的一侧面上紧贴设置铱镀层的钛阳极(钛阳极为3cm*3cm尺寸的钛片,铱镀层为二氧化铱,负载量为1mg/cm2),由此两个Nafion 115膜分别都设有铱镀层的钛阳极。阳极电解槽的顶部设有阳极排液排气口,供氧气产生排放使用,底部设有阳极进液口,供电解液的进入。阴极电解槽中部设有圆柱形砷单质催化剂电极,同时砷单质催化剂电极与阴极电解槽之间设有o型膨体四氟垫片。其反应具体条件为控制反应的电流为400、500和600mA,阴极电解槽及两个阳极电解槽内的电解液均为1M KOH溶液,阳极催化面积为9cm2,阴极催化剂面积为9.42cm2。The device structure is shown in Figure 1-2. The cathode electrolyzer is located between the two anode electrolyzers. A Nafion 115 membrane is provided between the cathode electrolyzers, which selectively transmits ions in the reaction process and has the function of separating the products of the cathode and cathode electrolyzers, thereby achieving absolute separation of explosive gases and realizing safe arsine production. An iridium-plated titanium anode (the titanium anode is a titanium sheet of 3cm*3cm in size, and the iridium-plated layer is iridium dioxide with a loading of 1mg/ cm2 ) is closely arranged on the side of the Nafion 115 membrane facing the anode electrolyzer, so that the two Nafion 115 membranes are respectively provided with an iridium-plated titanium anode. An anode liquid discharge outlet is provided at the top of the anode electrolyzer for oxygen generation and discharge, and an anode liquid inlet is provided at the bottom for the entry of electrolyte. A cylindrical arsenic single substance catalyst electrode is provided in the middle of the cathode electrolyzer, and an o-type expanded polytetrafluoroethylene gasket is provided between the arsenic single substance catalyst electrode and the cathode electrolyzer. The specific reaction conditions are as follows: the reaction current is controlled to be 400, 500 and 600 mA, the electrolyte in the cathode electrolytic cell and the two anode electrolytic cells is 1M KOH solution, the anode catalyst area is 9 cm 2 , and the cathode catalyst area is 9.42 cm 2 .
改变反应的条件进行测试,结果如表1。The reaction conditions were changed for testing, and the results are shown in Table 1.
表1.不同电流下氧气/砷烷产量Table 1. Oxygen/Arsine production at different currents
表1结果表明,本发明同时具有优异的氧气制备性能和砷烷的生产能力,具有良好的应用潜力。The results in Table 1 show that the present invention has both excellent oxygen preparation performance and arsine production capacity, and has good application potential.
实施例2:一种双阳极电催化制备砷烷的装置Example 2: A dual-anode electrocatalytic device for preparing arsine
实施例2的电解装置结构与实施例1中相同。反应具体条件为控制反应的电流为500mA,阴极电解槽及两个阳极电解槽内的电解液均为KOH溶液,阳极催化面积为9cm2,阴极催化剂面积为9.42cm2。The structure of the electrolysis device in Example 2 is the same as that in Example 1. The specific reaction conditions are that the current controlling the reaction is 500 mA, the electrolyte in the cathode electrolytic cell and the two anode electrolytic cells is KOH solution, the anode catalyst area is 9 cm 2 , and the cathode catalyst area is 9.42 cm 2 .
改变反应的条件进行测试,结果如表2.The reaction conditions were changed for testing, and the results are shown in Table 2.
表2.不同电解液浓度下氧气/砷烷产量Table 2. Oxygen/arsine production at different electrolyte concentrations
表2结果表明,本发明通过对电解液浓度的调整,可以实现砷烷产量的最优化条件筛选,当电解液浓度为1M时,其氧气和砷烷的产量最高,增加电解液浓度,产量有所降低,可能是由于析氢反应的影响。The results in Table 2 show that the present invention can achieve the optimal condition screening for arsine production by adjusting the electrolyte concentration. When the electrolyte concentration is 1 M, the production of oxygen and arsine is the highest. As the electrolyte concentration increases, the production decreases, which may be due to the influence of the hydrogen evolution reaction.
对比例1:单阳极电催化制备砷烷测试Comparative Example 1: Single anode electrocatalytic preparation of arsenic
装置结构参见图3,阴极电解槽位于阳极电解槽右侧,与阳极电解槽之间设有Nafion 115膜,选择性的透过反应过程中的离子,同时具有分离阴阳极电解槽产物的作用,达到爆炸气体的绝对分离,实现安全化砷烷生产。Nafion 115膜面向阳极电解槽的一侧面上紧贴设置铱镀层的钛阳极(钛阳极为3cm*3cm尺寸的钛片,铱镀层为二氧化铱,负载量为1mg/cm2)。阳极电解槽的顶部设有阳极排液排气口,供氧气产生排放使用,底部设有阳极进液口,供电解液的进入。阴极电解槽中部设有圆柱形砷单质催化剂电极,同时砷单质催化剂电极与阴极电解槽之间设有o型膨体四氟垫片。反应具体条件为控制反应的电流为500mA,阴极电解槽及阳极电解槽内的电解液均为1M KOH溶液,阳极催化面积为9cm2,阴极催化剂面积为9.42cm2。The device structure is shown in Figure 3. The cathode electrolyzer is located on the right side of the anode electrolyzer. A Nafion 115 membrane is provided between the cathode electrolyzer and the anode electrolyzer. It selectively transmits ions in the reaction process and has the function of separating the products of the cathode and cathode electrolyzers, achieving absolute separation of explosive gases and realizing safe arsine production. A titanium anode with an iridium coating is closely arranged on the side of the Nafion 115 membrane facing the anode electrolyzer (the titanium anode is a titanium sheet with a size of 3cm*3cm, and the iridium coating is iridium dioxide with a loading of 1mg/ cm2 ). An anode liquid discharge outlet is provided at the top of the anode electrolyzer for oxygen generation and discharge, and an anode liquid inlet is provided at the bottom for the entry of electrolyte. A cylindrical arsenic single substance catalyst electrode is provided in the middle of the cathode electrolyzer, and an o-type expanded polytetrafluoroethylene gasket is provided between the arsenic single substance catalyst electrode and the cathode electrolyzer. The specific reaction conditions are as follows: the reaction current is controlled to be 500 mA, the electrolyte in the cathode electrolytic cell and the anode electrolytic cell are both 1M KOH solution, the anode catalyst area is 9 cm 2 , and the cathode catalyst area is 9.42 cm 2 .
改变反应的条件进行测试,结果如表3.The reaction conditions were changed for testing, and the results are shown in Table 3.
表3.不同电流下氧气/砷烷产量Table 3. Oxygen/Arsine production at different currents
表3结果显示,电流为500mA/cm2时,制备砷烷的效果达到最佳。但相比于双阳极电催化制备砷烷装置,砷烷产生的效果降低50%-60%。该结果主要是由于双阳极的并联结构,提高了阳极的析氧的析氧能力,较于单电极,氧气的产生量提高一倍左右,该过程提高了反应过程的传质能力,大大提高了H+向阴极的传输速度和传输量,进一步提高了砷烷的产生速率。The results in Table 3 show that the effect of preparing arsine is best when the current is 500mA/ cm2 . However, compared with the dual-anode electrocatalytic arsine preparation device, the effect of arsine production is reduced by 50%-60%. This result is mainly due to the parallel structure of the dual anodes, which improves the oxygen evolution capacity of the anode. Compared with the single electrode, the amount of oxygen produced is increased by about one time. This process improves the mass transfer capacity of the reaction process, greatly increases the transmission speed and amount of H + to the cathode, and further increases the production rate of arsine.
本说明书所述的内容仅仅是对发明构思实现形式的列举,本发明的保护范围不应当被视为仅限于实施例所陈述的具体形式。The contents described in this specification are merely an enumeration of implementation forms of the inventive concept, and the protection scope of the present invention should not be regarded as being limited to the specific forms described in the embodiments.
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