CN113463126A - 一种非贵金属析氯催化剂电极及制备方法 - Google Patents
一种非贵金属析氯催化剂电极及制备方法 Download PDFInfo
- Publication number
- CN113463126A CN113463126A CN202110906283.6A CN202110906283A CN113463126A CN 113463126 A CN113463126 A CN 113463126A CN 202110906283 A CN202110906283 A CN 202110906283A CN 113463126 A CN113463126 A CN 113463126A
- Authority
- CN
- China
- Prior art keywords
- noble metal
- catalyst
- electrode
- chlorine evolution
- catalyst electrode
- 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
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 69
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 239000000460 chlorine Substances 0.000 title claims abstract description 50
- 229910052801 chlorine Inorganic materials 0.000 title claims abstract description 50
- 229910000510 noble metal Inorganic materials 0.000 title claims abstract description 26
- 238000002360 preparation method Methods 0.000 title abstract description 7
- 239000013535 sea water Substances 0.000 claims abstract description 19
- 239000000758 substrate Substances 0.000 claims abstract description 12
- 238000000034 method Methods 0.000 claims description 22
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 20
- 239000010936 titanium Substances 0.000 claims description 16
- 229910052719 titanium Inorganic materials 0.000 claims description 16
- 238000004070 electrodeposition Methods 0.000 claims description 5
- 230000003213 activating effect Effects 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 3
- 230000003287 optical effect Effects 0.000 claims description 2
- 238000004832 voltammetry Methods 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 230000003373 anti-fouling effect Effects 0.000 abstract description 7
- 230000002147 killing effect Effects 0.000 abstract description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 20
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 12
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 12
- 239000010409 thin film Substances 0.000 description 10
- 239000011780 sodium chloride Substances 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000004913 activation Effects 0.000 description 7
- 238000005868 electrolysis reaction Methods 0.000 description 7
- 238000004140 cleaning Methods 0.000 description 6
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 6
- 239000012153 distilled water Substances 0.000 description 6
- 238000001035 drying Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 229910052697 platinum Inorganic materials 0.000 description 6
- 238000004506 ultrasonic cleaning Methods 0.000 description 6
- 229910017052 cobalt Inorganic materials 0.000 description 5
- 239000010941 cobalt Substances 0.000 description 5
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 5
- 238000002441 X-ray diffraction Methods 0.000 description 4
- 239000002135 nanosheet Substances 0.000 description 4
- 230000003115 biocidal effect Effects 0.000 description 3
- 239000003139 biocide Substances 0.000 description 3
- 238000001878 scanning electron micrograph Methods 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- UBEWDCMIDFGDOO-UHFFFAOYSA-N cobalt(II,III) oxide Inorganic materials [O-2].[O-2].[O-2].[O-2].[Co+2].[Co+3].[Co+3] UBEWDCMIDFGDOO-UHFFFAOYSA-N 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 238000013112 stability test Methods 0.000 description 2
- PIILXFBHQILWPS-UHFFFAOYSA-N tributyltin Chemical compound CCCC[Sn](CCCC)CCCC PIILXFBHQILWPS-UHFFFAOYSA-N 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000010405 anode material Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000013480 data collection Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000006056 electrooxidation reaction Methods 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 230000005923 long-lasting effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/052—Electrodes comprising one or more electrocatalytic coatings on a substrate
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/467—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction
- C02F1/4672—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation
- C02F1/4674—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis by electrochemical disinfection; by electrooxydation or by electroreduction by electrooxydation with halogen or compound of halogens, e.g. chlorine, bromine
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/24—Halogens or compounds thereof
- C25B1/26—Chlorine; Compounds thereof
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/055—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material
- C25B11/057—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the substrate or carrier material consisting of a single element or compound
- C25B11/061—Metal or alloy
- C25B11/063—Valve metal, e.g. titanium
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B11/00—Electrodes; Manufacture thereof not otherwise provided for
- C25B11/04—Electrodes; Manufacture thereof not otherwise provided for characterised by the material
- C25B11/051—Electrodes formed of electrocatalysts on a substrate or carrier
- C25B11/073—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material
- C25B11/075—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound
- C25B11/077—Electrodes formed of electrocatalysts on a substrate or carrier characterised by the electrocatalyst material consisting of a single catalytic element or catalytic compound the compound being a non-noble metal oxide
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/46—Treatment of water, waste water, or sewage by electrochemical methods
- C02F1/461—Treatment of water, waste water, or sewage by electrochemical methods by electrolysis
- C02F1/46104—Devices therefor; Their operating or servicing
- C02F1/46109—Electrodes
- C02F2001/46133—Electrodes characterised by the material
- C02F2001/46138—Electrodes comprising a substrate and a coating
- C02F2001/46142—Catalytic coating
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/08—Seawater, e.g. for desalination
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Organic Chemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- General Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Electrodes For Compound Or Non-Metal Manufacture (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
本发明属于海洋污损防护技术领域,具体涉及一种非贵金属析氯催化剂电极及制备方法。非贵金属析氯催化剂电极,包括基体,所述基体表面沉积催化剂Co(OH)2。本发明负载电解海水析氯的非贵金属催化剂的电极可以显著提高电解海水的效率,并且可以在短时间、小电压的通电情况下产生足量且可控制的具有生物杀灭作用的有效氯,从而达到防污的效果。
Description
技术领域
本发明属于海洋污损防护技术领域,具体涉及一种非贵金属析氯催化剂电极及制备方法。
背景技术
海洋生物污损问题是一个长期困扰人类的问题,它给海洋探索过程中使用的各种设备带来了诸多的负面影响,例如降低船舶航行速度、堵塞冷却水通道以及影响水下传感器数据收集的准确性。这也刺激了人们对海洋设备的防污损技术的开发。目前,市场上用于防污的手段主要有以下三种:(1)纯粹的机械设备,例如刮刀;(2)基于铜和三丁基锡生物杀灭剂浸出系统;(3)基于局部电解海水活性氯生成的生物杀灭剂生成系统。机械防污在进行几个操作周期以后需要人工维护,不适合远程设备的使用。三丁基锡防污具有长效性,但是对海洋环境有巨大的危害。电化学氯化局部生成生物杀灭剂因其操作简单、可控性强成为最有前景的海洋防污技术。
电解海水制氯关键的就是电解析氯所用的阳极材料。而电解海水与氯碱工业的电解产氯技术不同,电解海水过程中氯离子浓度低,且作为电解质的海水呈现近中性,使得在电解的过程中不仅有析氯反应,同时还伴随着大量的析氧反应。目前成熟的商业级析氯电极-DSA电极仅仅解决了电解高浓度氯离子的问题,对于电解海水还存在低选择性和低稳定性等问题。此外,目前针对电解海水析氯的催化剂大多都还是基于贵金属及其氧化物的研究,由于高成本使得其应用受限。
因此,开发低成本、高活性的电解海水析氯催化剂有助于进一步推动电解海水析氯技术在海洋防污方向的应用。
发明内容
本发明的目的是提供一种具有优异析氯性能的非贵金属析氯催化剂电极及制备方法,以解决现有析氯电极存在的问题和缺陷。
为了实现上述目的,本发明提供的其中一种技术方案为:一种非贵金属析氯催化剂电极,包括基体,所述基体表面沉积有Co(OH)2催化剂。
作为本发明的一种优选方式,所述的基体为金属钛。
为了实现本发明的目的,本发明还提供了上述非贵金属析氯催化剂电极的制备方法,该方法包括:
在Co(NO3)2溶液中,采用阴极恒电压法在基体表面制备析氯催化剂Co(OH)2,得到催化剂电极;
采用线性伏安扫描法对所述基体表面的催化剂进行活化处理。
进一步优选地,所述阴极恒电压法实现的温度为0~50℃,电沉积时间为10s~900s。
进一步优选地,线性伏安扫描的电压为0.55~1.55 V。
本发明还提供上述非贵金属析氯催化剂电极的应用,所述催化剂电极作为阳极,其作为催化剂阳极电解海水制氯,用于水下光学窗口防污。
与现有技术相比,本发明具有如下有益效果:
本发明负载电解海水析氯的非贵金属催化剂的电极可以显著提高电解海水的效率,并且可以在短时间、小电压的通电情况下产生足量且可控制的具有生物杀灭作用的有效氯,从而达到防污的效果。本发明的非贵金属析氯催化剂电极的制备过程简单,并且通过对催化剂的活化处理,提高其电催化活性,制备方法所使用的实验的仪器和药品也容易获得,对环境无危害。
附图说明
图1为实例1方法制备的钴基薄膜催化剂的X射线衍射图(XRD);
图2为实例1方法制备的钴基薄膜催化剂的扫描电镜图(SEM);(a)活化处理前;(b)活化处理后;
图3为实例1方法制备的钴基薄膜催化剂在3.5% NaCl 和中性饱和NaCl溶液中的线性扫描曲线,扫描速率10 mV/s;
图4为实例1方法制备的钴基薄膜催化剂电极和商用析氯电极DSA在3.5% NaCl 溶液中的线性扫描曲线,扫描速率10 mV/s;
图5为实例1方法制备的钴基薄膜催化剂的稳定性测试图。
具体实施方式
为了便于理解本发明,下面结合附图和具体实施例,对本发明进行更详细的说明。附图中给出了本发明的较佳的实施例。但是,本发明可以以许多不同的形式来实现,并不限于本说明书所描述的实施例。相反地,提供这些实施例的目的是使对本发明公开内容的理解更加透彻全面。
实施例1 本实施例提供的非贵金属析氯催化剂电极,主要由括钛网和钛网表面的薄膜催化剂Co(OH)2构成。
本实施例的非贵金属析氯催化剂电极,采用阴极恒电压电沉积法制备,具体包括以下步骤:
(1)将纯度为99.99%的钛网按1cm×1cm进行切割,用蒸馏水冲洗钛网的表面。冲洗干净以后,用无水乙醇对其进行超声清洗20 min,清洗结束后将无水乙醇倒掉换成蒸馏水进行20 min的超声清洗,清洗完毕后放入60 ℃的烘箱中使其表面快速干燥。
(2)将处理好的钛网用电极夹夹好,作为工作电极,另外铂网和饱和甘汞电极分别作为对电极和参比电极,将其放入25℃ 60 mL 0.1M Co(NO3)2溶液中,在电极间施加-1 V(vs. SCE)的恒定电压,维持850s,停止后取下工作电极,在室温下干燥,所制得的Co(OH)2析氯催化剂负载在钛网上。
(3)将上述制得的电极作为工作电极,铂网和饱和甘汞电极张分别作为对电极和参比电极,放入60 mL 3.5% NaCl 溶液中,在室温下进行线性扫描,扫描速率为10 mV/s,从0.55 V(vs. SCE)开始扫到1.55 V(vs. SCE)停止,取出电极室温下干燥,完成催化剂活化。
对本实施例制备的催化剂电极进行X射线衍射测定,如图1所示,根据XRD图可以确定所制备的析氯催化剂的主要成分是Co(OH)2。
图2 为本实施例制备的Co(OH)2电解海水析氯催化剂的SEM图。根据SEM图可以清楚的看出,Co(OH)2析氯催化剂电极表面呈现多层的纳米片结构,而且在活化处理前表面的纳米片较为团聚密集,而在活化处理之后催化剂表面微结构变得较为疏松,这无疑使得比表面积增大,从而其电催化活性也增大。另外,经过电化学氧化的纳米片厚度增大,其结构变得更加的稳定。
本对实施例制备的催化剂电极的电催化活性进行测试:
对比例采用以Co3O4为催化剂的电极。图3 为本实施例制备的Co(OH)2薄膜催化剂电极与Co3O4电极(Co3O4电极参照专利公开文献202110050042.6中的方法制备)分别在3.5%NaCl和饱和NaCl溶液中的线性扫描曲线,从曲线中可以看出,无论是在低浓度还是高浓度的NaCl溶液中,本实施制备的Co(OH)2薄膜催化剂具有优异的电催化活性,且均优于对比例的Co3O4电极。
图4为本实施例制备的Co(OH)2电解海水析氯催化剂阳极和商用析氯电极DSA在3.5% NaCl溶液中的线性扫描曲线,可以看出本实施例所制备Co(OH)2薄膜催化剂电极电解海水析氯性能优于商用DSA电极。
图5 为本实施例制备的Co(OH)2电解海水析氯催化剂在3.5% NaCl溶液中的稳定性测试,从图中曲线可以看出,所制备的非贵金属催化剂Co(OH)2具有优异的稳定性。
实施例2 本实施例提供的非贵金属析氯催化剂电极,主要由括钛片和钛片表面的薄膜催化剂Co(OH)2构成。
本实施例的非贵金属析氯催化剂电极,采用阴极恒电压电沉积法制备,具体包括以下步骤:
(1)将钛片按1cm×1cm进行切割,用蒸馏水冲洗钛片的表面。冲洗干净以后,用无水乙醇对其进行超声清洗20 min,清洗结束后将无水乙醇倒掉换成蒸馏水进行20 min的超声清洗,清洗完毕后放入60 ℃的烘箱中使其表面快速干燥。
(2)将处理好的钛片用电极夹夹好,作为工作电极,另外铂网和饱和甘汞电极分别作为对电极和参比电极,将其放入50℃ 60 mL 0.1M Co(NO3)2溶液中,在电极间施加-1 V(vs. SCE)的恒定电压,维持400s,停止后取下工作电极,在室温下干燥,所制得的Co(OH)2析氯催化剂负载在钛片上。
(3)将上述制得的电极作为工作电极,铂网和饱和甘汞电极张分别作为对电极和参比电极,放入60 mL 3.5% NaCl 溶液中在室温下进行线性扫描,扫描速率为10 mV/s,从0.55 V(vs. SCE)开始扫到1.55 V(vs. SCE)停止,取出电极室温下干燥,完成催化剂活化。
实施例3 本实施例提供的非贵金属析氯催化剂电极,主要由钛片和钛片表面的催化剂Co(OH)2构成。
本实施例的非贵金属析氯催化剂电极,采用阴极恒电压电沉积法制备,具体包括以下步骤:
(1)将钛片按1cm×1cm进行切割,用蒸馏水冲洗钛片的表面。冲洗干净以后,用无水乙醇对其进行超声清洗20 min,清洗结束后将无水乙醇倒掉换成蒸馏水进行20 min的超声清洗,清洗完毕后放入60 ℃的烘箱中使其表面快速干燥。
(2)将处理好的钛片用电极夹夹好,作为工作电极,另外铂网和饱和甘汞电极分别作为对电极和参比电极,将其放入25℃ 60 mL 0.1M Co(NO3)2溶液中,在电极间施加-1 V(vs. SCE)的恒定电压,维持600s,停止后取下工作电极,在室温下干燥,所制得的Co(OH)2析氯催化剂负载在钛片上。
(3)将上述制得的电极作为工作电极,铂网和饱和甘汞电极张分别作为对电极和参比电极,放入60 mL 3.5% NaCl 溶液中在室温下进行线性扫描,扫描速率为10 mV/s,从0.55 V(vs. SCE)开始扫到1.55 V(vs. SCE)停止,取出电极室温下干燥,完成催化剂活化。
Claims (6)
1.一种非贵金属析氯催化剂电极,包括基体,其特征在于:所述基体表面沉积有催化剂Co(OH)2。
2.根据权利要求1所述的非贵金属析氯催化剂电极,其特征在于:所述的基体为金属钛。
3.一种如权利要求1或2所述的非贵金属析氯催化剂电极的制备方法,其特征在于:在Co(NO3)2溶液中,采用阴极恒电压法在基体表面制备析氯催化剂Co(OH)2,得到催化剂电极;
采用线性伏安扫描法对所述基体表面的催化剂进行活化处理。
4.根据权利要求3所述的非贵金属析氯催化剂电极的制备方法,其特征在于:所述阴极恒电压法实现的温度为0~50℃,电沉积时间为10s~900s。
5.根据权利要求3所述的非贵金属析氯催化剂电极的制备方法,其特征在于:线性伏安扫描的电压范围为0.55~1.55 V。
6.一种如权利要求1或2所述的非贵金属析氯催化剂电极的应用,其特征在于:其作为催化剂阳极电解海水制氯,用于水下光学窗口防污。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110906283.6A CN113463126B (zh) | 2021-08-09 | 2021-08-09 | 一种非贵金属析氯催化剂电极及制备方法 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110906283.6A CN113463126B (zh) | 2021-08-09 | 2021-08-09 | 一种非贵金属析氯催化剂电极及制备方法 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN113463126A true CN113463126A (zh) | 2021-10-01 |
CN113463126B CN113463126B (zh) | 2023-10-24 |
Family
ID=77867624
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110906283.6A Active CN113463126B (zh) | 2021-08-09 | 2021-08-09 | 一种非贵金属析氯催化剂电极及制备方法 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN113463126B (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113529132A (zh) * | 2021-08-09 | 2021-10-22 | 中国科学院海洋研究所 | 一种钴基催化剂电极及其制备方法 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107236964A (zh) * | 2017-05-10 | 2017-10-10 | 东北大学 | 一种氯化钴电转化直接制备氢氧化钴的方法 |
CN112899715A (zh) * | 2021-01-14 | 2021-06-04 | 山东大学 | 一种氧化钴纳米薄片析氯电极及其制备方法与应用 |
-
2021
- 2021-08-09 CN CN202110906283.6A patent/CN113463126B/zh active Active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107236964A (zh) * | 2017-05-10 | 2017-10-10 | 东北大学 | 一种氯化钴电转化直接制备氢氧化钴的方法 |
CN112899715A (zh) * | 2021-01-14 | 2021-06-04 | 山东大学 | 一种氧化钴纳米薄片析氯电极及其制备方法与应用 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113529132A (zh) * | 2021-08-09 | 2021-10-22 | 中国科学院海洋研究所 | 一种钴基催化剂电极及其制备方法 |
Also Published As
Publication number | Publication date |
---|---|
CN113463126B (zh) | 2023-10-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Chen et al. | Corrosion resistance mechanism of a novel porous Ti/Sn-Sb-RuOx/β-PbO2 anode for zinc electrowinning | |
US10975482B1 (en) | Self-derivative iron-containing nickel anode for water electrolysis | |
Pak | Ti plate with TiO2 nanotube arrays as a novel cathode for nitrate reduction | |
JP5518900B2 (ja) | 水又はアルカリ金属化合物の水溶液の電気分解用の陰極、アルカリ金属塩化物の電気分解用電解槽、及び水又はアルカリ金属化合物の水溶液の電気分解用の陰極の製造方法 | |
US8425740B2 (en) | Cathode for hydrogen generation and method for producing the same | |
US3977958A (en) | Insoluble electrode for electrolysis | |
EP2765222A1 (de) | Katalysatorbeschichtung und Verfahren zu ihrer Herstellung | |
Spasojević et al. | Microstructure of new composite electrocatalyst and its anodic behavior for chlorine and oxygen evolution | |
CN108328703B (zh) | 钛基二氧化钛纳米管沉积锡锑氟电极的制备及其对电镀铬废水中铬抑雾剂降解的应用 | |
CN111286751A (zh) | 一种基于核壳结构的钌铱系钛基金属氧化物电极材料、其制备方法及应用 | |
CN109576733B (zh) | 一种碳纤维负载的析氯催化电极的制备方法 | |
CN113463126B (zh) | 一种非贵金属析氯催化剂电极及制备方法 | |
Huang et al. | Effect of precursor baking on the electrochemical properties of IrO2-Ta2O5/Ti anodes | |
Hosseini et al. | Evaluation of the Performance of Platinum Nanoparticle–Titanium Oxide Nanotubes as a New Refreshable Electrode for Formic Acid Electro‐oxidation | |
CN112899715B (zh) | 一种氧化钴纳米薄片析氯电极及其制备方法与应用 | |
Abbar et al. | A kinetic study of oxalic acid electrochemical oxidation on a manganese dioxide rotating cylinder anode | |
Brudzisz et al. | A facile approach to silver nanowire array electrode preparation and its application for chloroform reduction | |
CN113699540B (zh) | 一种消毒液的制备方法 | |
CN113529132A (zh) | 一种钴基催化剂电极及其制备方法 | |
JP7133661B2 (ja) | 水分解酸素発生用のポリチオフェン系化合物/炭素繊維布電極及びその製造方法 | |
Ravichandran et al. | Indirect electroreduction of o-nitrophenol to o-aminophenol on titanium dioxide coated titanium electrodes | |
JP7376913B2 (ja) | 電気分解装置 | |
CN115125562B (zh) | 一种电解生成次氯酸的复合电极及制备与应用 | |
KR102648323B1 (ko) | 선박평형수 전기분해용 Pt-Ru-Ti 촉매 전극 | |
CN110217861B (zh) | 一种长寿命多孔钛基二氧化铅电极材料的制备及应用 |
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 | ||
GR01 | Patent grant | ||
GR01 | Patent grant |