CN103539227A - Preparation Technology of Ag-doped MnO2-CeO2 Active Alumina Particle Electrode Containing CuO Interlayer - Google Patents
Preparation Technology of Ag-doped MnO2-CeO2 Active Alumina Particle Electrode Containing CuO Interlayer Download PDFInfo
- Publication number
- CN103539227A CN103539227A CN201310525735.1A CN201310525735A CN103539227A CN 103539227 A CN103539227 A CN 103539227A CN 201310525735 A CN201310525735 A CN 201310525735A CN 103539227 A CN103539227 A CN 103539227A
- Authority
- CN
- China
- Prior art keywords
- solution
- granular substance
- hours
- concentration
- add
- 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
Landscapes
- Catalysts (AREA)
Abstract
本发明公开了含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极的制备工艺。将AgNO3加到异丙醇中得到溶液A,将处理后的Al2O3加到溶液A中,过滤得到颗粒B和微乳液X,用乙醇洗涤后得到颗粒D;将颗粒D加到X中过滤后得到颗粒F。利用Ce(NO3)2、CuCl2、MnCl2制备溶液B1、B2、B3、B4、B5、C、D、E、F。将颗粒F依次经过溶液B1、B2、B3、B4、B5处理后得到颗粒I。将颗粒I加到溶液C中,过滤后用乙醇洗涤并干燥得到颗粒K。将颗粒K加到溶液D中,过滤后用乙醇洗涤并干燥得到颗粒M。将M加到溶液E中,过滤后用乙醇洗涤并干燥得到颗粒O。将颗粒O加到溶液F中,过滤后用乙醇洗涤,干燥并在580℃条件下焙烧4h,即得到含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极。The invention discloses a preparation process of an Ag-doped MnO 2 -CeO 2 active alumina particle electrode containing a CuO intermediate layer. Add AgNO3 to isopropanol to obtain solution A, add treated Al2O3 to solution A, filter to obtain particle B and microemulsion X, and obtain particle D after washing with ethanol; add particle D to X Particle F was obtained after medium filtration. Solutions B 1 , B 2 , B 3 , B 4 , B 5 , C, D, E, F were prepared using Ce(NO 3 ) 2 , CuCl 2 , MnCl 2 . Particle F is treated with solutions B 1 , B 2 , B 3 , B 4 , and B 5 in sequence to obtain particle I. Particle I was added to solution C, filtered, washed with ethanol and dried to obtain Particle K. Particle K was added to solution D, filtered, washed with ethanol and dried to obtain particle M. M was added to solution E, filtered, washed with ethanol and dried to obtain particle O. Add particles O to solution F, filter, wash with ethanol, dry and bake at 580°C for 4 hours to obtain an Ag-doped MnO 2 -CeO 2 active alumina particle electrode containing a CuO interlayer.
Description
技术领域technical field
本发明属于电催化氧化法处理废水的化学修饰电极技术领域,特别涉及一种含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极的制备工艺。The invention belongs to the technical field of chemically modified electrodes for treating wastewater by an electrocatalytic oxidation method, and in particular relates to a preparation process of an Ag-doped MnO 2 -CeO 2 active alumina particle electrode containing a CuO intermediate layer.
背景技术Background technique
电催化氧化技术通过产生羟基自由基等强氧化性的活性基团来降解废水中的有机污染物,在处理高浓度、难生化降解废水方面具有无二次污染、成本低、适用性强、效率高等特点,其中三维电催化氧化技术,通过在二维电极的阳极和阴极之间加入具有催化活性的粒子电极,通过某种方式使填充的粒状电极表面带电,改善了二维电极的其有效面积小、传质效果差、电流效率低等缺陷,适用于各种浓度的废水,即使对污染物浓度很低的废水也有较好的处理效果,是目前研究较多的一种电催化氧化水处理技术。将三维电极法应用于废水处理,其处理效果不仅与主电极性能密切相关,而且和粒子电极的性能有很大关系,因此如何提高粒子电极的催化性能成为了近年来研究的热点。Electrocatalytic oxidation technology degrades organic pollutants in wastewater by generating strong oxidizing active groups such as hydroxyl radicals. It has no secondary pollution, low cost, strong applicability, and high efficiency in treating high-concentration, biodegradable wastewater. Advanced features, in which three-dimensional electrocatalytic oxidation technology, by adding a catalytically active particle electrode between the anode and cathode of the two-dimensional electrode, the surface of the filled granular electrode is charged in a certain way, and the effective area of the two-dimensional electrode is improved. Small, poor mass transfer effect, low current efficiency and other defects, it is suitable for various concentrations of wastewater, even for wastewater with low pollutant concentration, it has a good treatment effect, and it is a kind of electrocatalytic oxidation water treatment that has been studied more at present. technology. The application of the three-dimensional electrode method to wastewater treatment is not only closely related to the performance of the main electrode, but also closely related to the performance of the particle electrode. Therefore, how to improve the catalytic performance of the particle electrode has become a research hotspot in recent years.
常用的粒子电极材料主要有金属导体、金属氧化物、镀有金属层的玻璃球或塑料球、石墨粒子、活性氧化铝粒子、碳纤维材料以及活性炭颗粒等。传统电极的电阻较大、导电率低是使得其在废水处理中电流效率低、稳定性不够、寿命短、电极材料成本较高,而且电极制备工艺复杂,限制了粒子电极材料的发展,所以新型粒子电极材料的研究还需要进一步加强。近些年采用浸渍-热分解法制备负载型粒子电极受到越来越多的学者重视,但是存在着重复使用效果差、电极效率低等缺点,目前还缺少粒子电极制备工艺方面的研究。Commonly used particle electrode materials mainly include metal conductors, metal oxides, glass or plastic balls coated with metal layers, graphite particles, activated alumina particles, carbon fiber materials, and activated carbon particles. The large resistance and low conductivity of traditional electrodes make it low current efficiency, insufficient stability, short life, high cost of electrode materials in wastewater treatment, and the electrode preparation process is complicated, which limits the development of particle electrode materials. Therefore, the new The research on particle electrode materials still needs to be further strengthened. In recent years, the preparation of supported particle electrodes by impregnation-thermal decomposition has attracted more and more attention from scholars, but there are disadvantages such as poor reusability and low electrode efficiency, and there is still a lack of research on the preparation process of particle electrodes.
发明内容Contents of the invention
本发明的目的是提供一种含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极的制备工艺。其具体步骤如下:The object of the present invention is to provide a preparation process of an Ag-doped MnO 2 -CeO 2 active alumina particle electrode containing a CuO intermediate layer. The specific steps are as follows:
(1)将300g粒径为3-5mm的γ-Al2O3球用500ml去离子水洗涤,重复洗涤3次,然后放入200ml无水乙醇中浸泡10h,用500ml去离子水清洗1次后,在80℃条件下干燥10h,得到颗粒物质A;(1) Wash 300g of γ-Al 2 O 3 balls with a particle size of 3-5mm with 500ml of deionized water, repeat the washing 3 times, then soak in 200ml of absolute ethanol for 10h, and wash once with 500ml of deionized water Afterwards, drying at 80°C for 10 hours to obtain granular substance A;
(2)将50ml浓度为0.5mol/L的AgNO3加入150ml异丙醇中,得到溶液A;(2) Add 50ml of AgNO with a concentration of 0.5mol/L into 150ml of isopropanol to obtain solution A;
(3)将步骤(1)得到的颗粒物质A加入步骤(2)得到的溶液A中,并在摇床中摇动3h,过滤得到颗粒物质B和微乳液X,用100mL质量浓度为95%的乙醇洗涤颗粒物质B,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质C;(3) Add the granular substance A obtained in step (1) to the solution A obtained in step (2), and shake it in a shaker for 3h, filter to obtain granular substance B and microemulsion X, and use 100mL of 95% mass concentration Wash the granular substance B with ethanol, repeat the washing twice, and then dry at 80°C for 10 hours to obtain granular substance C;
(4)将步骤(3)得到的颗粒物质C置于马弗炉中在500℃条件下焙烧4h,得到颗粒物质D;(4) The granular substance C obtained in step (3) is placed in a muffle furnace and roasted at 500° C. for 4 hours to obtain the granular substance D;
(5)将步骤(4)得到的颗粒物质D加入步骤(3)得到的微乳液X中,并在摇床中摇动3h,过滤除去液体得到颗粒物质E,用100mL质量浓度为95%的乙醇洗涤颗粒物质E,重复洗涤2次,然后在80℃条件下干燥10h,然后置于马弗炉中在500℃条件下焙烧4h,得到颗粒物质F;(5) Add the granular substance D obtained in step (4) to the microemulsion X obtained in step (3), and shake it in a shaker for 3h, filter and remove the liquid to obtain granular substance E, and use 100mL of ethanol with a mass concentration of 95% Washing the granular substance E, repeating the washing twice, then drying at 80°C for 10 hours, and then roasting in a muffle furnace at 500°C for 4 hours to obtain granular substance F;
(6)将10ml浓度为0.5mol/L的Ce(NO3)2溶液和100ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入10ml浓度为0.5mol/L的MnCl2溶液,摇匀后分成等量5份,得到溶液B1、溶液B2、溶液B3、溶液B4、溶液B5;(6) 10ml concentration is 0.5mol/L Ce(NO 3 ) 2 solution and 100ml concentration is 0.5mol/L CuCl 2 solution joins in 120ml isopropanol and 5ml concentrated hydrochloric acid, then adds 10ml concentration and is 0.5mol /L MnCl 2 solution, shake well and divide into 5 equal parts to obtain solution B 1 , solution B 2 , solution B 3 , solution B 4 , and solution B 5 ;
(7)将步骤(5)得到的颗粒物质F加入步骤(6)得到的溶液B1中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G1,用100mL质量浓度为95%的乙醇洗涤颗粒物质G1,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H1;(7) Add the granular substance F obtained in step (5) to the solution B 1 obtained in step (6), shake it in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G1, and use 100mL of ethanol with a mass concentration of 95% washing the granular substance G1, repeating the washing twice, and then drying at 80° C. for 10 hours to obtain the granular substance H 1 ;
(8)将步骤(7)得到的颗粒物质H1加入步骤(6)得到的溶液B2中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G2,用100mL质量浓度为95%的乙醇洗涤颗粒物质G2,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H2;(8) Add the granular substance H 1 obtained in step (7) to the solution B 2 obtained in step (6), shake it in a shaker for 3 hours, remove the liquid by filtration to obtain granular substance G2, and use 100 mL of washing the granular substance G2 with ethanol, repeating the washing twice, and then drying at 80°C for 10 hours to obtain the granular substance H 2 ;
(9)将步骤(8)得到的颗粒物质H2加入步骤(6)得到的溶液B3中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G3,用100mL质量浓度为95%的乙醇洗涤颗粒物质G3,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H3;(9) Add the granular substance H2 obtained in step (8) to the solution B3 obtained in step (6), shake it in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G3, and use 100mL of 95% mass concentration washing the granular substance G3 with ethanol, repeating the washing twice, and then drying at 80° C. for 10 hours to obtain the granular substance H 3 ;
(10)将步骤(9)得到的颗粒物质H3加入步骤(6)得到的溶液B4中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G4,用100mL质量浓度为95%的乙醇洗涤颗粒物质G4,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H4;(10) Add the granular substance H3 obtained in step (9) to the solution B4 obtained in step (6), and shake it in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G4, and use 100mL of washing the granular substance G4 with ethanol, repeating the washing twice, and then drying at 80°C for 10 hours to obtain the granular substance H 4 ;
(11)将步骤(10)得到的颗粒物质H4加入步骤(6)得到的溶液B5中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G5,用100mL质量浓度为95%的乙醇洗涤颗粒物质G5,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H5;将H5置于马弗炉中在580℃条件下焙烧4h,得到颗粒物质I;(11) Add the granular substance H4 obtained in step (10) to the solution B5 obtained in step (6), and shake it in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G5, and use 100mL of Wash the granular substance G5 with ethanol, repeat the washing twice, and then dry at 80°C for 10 hours to obtain granular substance H5 ; place H5 in a muffle furnace and roast at 580°C for 4 hours to obtain granular substance I;
(12)将20ml浓度为0.5mol/L的Ce(NO3)2溶液和80ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入20ml浓度为0.5mol/L的MnCl2溶液,得到溶液C;(12) 20ml concentration is 0.5mol/L Ce(NO 3 ) 2 solution and 80ml concentration is 0.5mol/L CuCl 2 solution joins in 120ml isopropanol and 5ml concentrated hydrochloric acid, then adds 20ml concentration is 0.5mol /L of MnCl solution to obtain solution C;
(13)将步骤(11)得到的颗粒物质I加入步骤(12)得到的溶液C中,并在摇床中摇动3h;过滤除去液体得到颗粒物质J,用100mL质量浓度为95%的乙醇洗涤颗粒物质J,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质K;(13) Add the granular substance I obtained in step (11) to the solution C obtained in step (12), and shake it in a shaker for 3 hours; filter and remove the liquid to obtain granular substance J, wash with 100 mL of ethanol with a mass concentration of 95% For granular substance J, repeat washing twice, and then dry at 80°C for 10 hours to obtain granular substance K;
(14)将40ml浓度为0.5mol/L的Ce(NO3)2溶液和40ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入40ml浓度为0.5mol/L的MnCl2溶液,得到溶液D;(14) 40ml concentration is 0.5mol/L Ce(NO 3 ) 2 solution and 40ml concentration is 0.5mol/L CuCl 2 solution is added in 120ml isopropanol and 5ml concentrated hydrochloric acid, then add 40ml concentration is 0.5mol /L of MnCl solution to obtain solution D;
(15)将步骤(13)得到的颗粒物质K加入步骤(14)得到的溶液D中,并在摇床中摇动3h;过滤除去液体得到颗粒物质L,用100mL质量浓度为95%的乙醇洗涤颗粒物质L,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质M;(15) Add the granular substance K obtained in step (13) to the solution D obtained in step (14), and shake it in a shaker for 3 hours; filter and remove the liquid to obtain granular substance L, wash with 100 mL of ethanol with a mass concentration of 95% The granular substance L was repeatedly washed twice, and then dried at 80°C for 10 hours to obtain the granular substance M;
(16)将45ml浓度为0.5mol/L的Ce(NO3)2溶液和l5ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入60ml浓度为0.5mol/L的MnCl2溶液,得到溶液E;(16) 45ml concentration is 0.5mol/L Ce(NO 3 ) 2 solution and 15ml concentration is 0.5mol/L CuCl 2 solution joins in 120ml isopropanol and 5ml concentrated hydrochloric acid, then adds 60ml concentration and is 0.5mol /L of MnCl solution to obtain solution E;
(17)将步骤(15)得到的颗粒物质M加入步骤(16)得到的溶液E中,并在摇床中摇动3h;过滤除去液体得到颗粒物质N,用100mL质量浓度为95%的乙醇洗涤颗粒物质N,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质O;(17) Add the particulate matter M obtained in step (15) to the solution E obtained in step (16), and shake it in a shaker for 3 hours; filter and remove the liquid to obtain particulate matter N, wash with 100 mL of ethanol with a mass concentration of 95% For granular substance N, repeat washing twice, and then dry at 80°C for 10 hours to obtain granular substance O;
(18)将15ml浓度为0.5mol/L的Ce(NO3)2溶液和5ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入100ml浓度为0.5mol/L的MnCl2溶液,得到溶液F;(18) 15ml concentration is 0.5mol/L Ce(NO 3 ) 2 solution and 5ml concentration is 0.5mol/L CuCl 2 solution joins in 120ml isopropanol and 5ml concentrated hydrochloric acid, then adds 100ml concentration is 0.5mol /L of MnCl solution to obtain solution F;
(19)将步骤(17)得到的颗粒物质O加入步骤(18)得到的溶液F中,并在摇床中摇动3h;过滤除去液体得到颗粒物质P,用100mL质量浓度为95%的乙醇洗涤颗粒物质P,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质Q,将Q置于马弗炉中在580℃条件下焙烧4h,得到的颗粒物质即为含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极。(19) Add the particulate substance O obtained in step (17) to the solution F obtained in step (18), and shake it in a shaker for 3 hours; filter and remove the liquid to obtain particulate substance P, wash with 100 mL of ethanol with a mass concentration of 95% The granular substance P was repeatedly washed twice, and then dried at 80°C for 10 hours to obtain the granular substance Q, which was placed in a muffle furnace and roasted at 580°C for 4 hours, and the obtained granular substance was the CuO-containing interlayer. Loading Ag-doped MnO 2 -CeO 2 active alumina particle electrode.
本发明的有益效果是,制得的含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极具有电流效率高、稳定性强、电极寿命长等特点。The beneficial effect of the invention is that the prepared Ag-doped MnO 2 -CeO 2 activated alumina particle electrode containing the CuO intermediate layer has the characteristics of high current efficiency, strong stability, long electrode life and the like.
具体实施方式Detailed ways
本发明提供一种含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极的制备工艺,下面通过一个实例来说明其实施过程。The invention provides a preparation process of an Ag-doped MnO 2 -CeO 2 active alumina particle electrode containing a CuO intermediate layer, and an example is used to illustrate the implementation process.
实施例1.Example 1.
将300g粒径为3-5mm的γ-Al2O3球用500ml去离子水洗涤,重复洗涤3次,然后放入200ml无水乙醇中浸泡10h,用500ml去离子水清洗1次后,在80℃条件下干燥10h,得到颗粒物质A。Wash 300g of γ-Al 2 O 3 spheres with a particle size of 3-5mm with 500ml of deionized water, repeat the washing 3 times, then soak in 200ml of absolute ethanol for 10h, wash once with 500ml of deionized water, and then Dry at 80° C. for 10 h to obtain granular substance A.
将50ml浓度为0.5mol/L的AgNO3加入150ml异丙醇中,得到溶液A。将颗粒物质A加入到溶液A中,并在摇床中摇动3h,过滤得到颗粒物质B和微乳液X,用100mL质量浓度为95%的乙醇洗涤颗粒物质B,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质C;将颗粒物质C置于马弗炉中在500℃条件下焙烧4h,得到颗粒物质D;将颗粒物质D加入到微乳液X中,并在摇床中摇动3h,过滤除去液体得到颗粒物质E,用100mL质量浓度为95%的乙醇洗涤E,重复洗涤2次,然后在80℃条件下干燥10h,然后置于马弗炉中在500℃条件下焙烧4h,得到颗粒物质F。Add 50ml of AgNO3 with a concentration of 0.5mol/L into 150ml of isopropanol to obtain solution A. Add granular substance A to solution A, shake in a shaker for 3 h, filter to obtain granular substance B and microemulsion X, wash granular substance B with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then wash at 80 Dry at ℃ for 10 hours to obtain granular substance C; put granular substance C in a muffle furnace and roast at 500°C for 4 hours to obtain granular substance D; add granular substance D to microemulsion X, and Shake for 3 hours, remove the liquid by filtration to obtain particulate matter E, wash E with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, then dry at 80 °C for 10 h, and then place it in a muffle furnace for roasting at 500 °C 4h, the particulate matter F was obtained.
将10ml浓度为0.5mol/L的Ce(NO3)2溶液和100ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入10ml浓度为0.5mol/L的MnCl2溶液,摇匀后分成等量5份,得到溶液B1、溶液B2、溶液B3、溶液B4、溶液B5;Add 10ml of Ce(NO 3 ) solution with a concentration of 0.5mol/L and 100ml of a CuCl solution with a concentration of 0.5mol/L into 120ml of isopropanol and 5ml of concentrated hydrochloric acid, and then add 10ml of a solution with a concentration of 0.5mol/L The MnCl 2 solution was shaken and divided into 5 equal parts to obtain solution B 1 , solution B 2 , solution B 3 , solution B 4 , and solution B 5 ;
将颗粒物质F加入到溶液B1中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G1,用100mL质量浓度为95%的乙醇洗涤颗粒物质G1,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H1;将颗粒物质H1加入到溶液B2中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G2,用100mL质量浓度为95%的乙醇洗涤颗粒物质G2,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H2;将颗粒物质H2加入到溶液B3中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G3,用100mL质量浓度为95%的乙醇洗涤颗粒物质G3,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H3;将颗粒物质H3加入到溶液B4中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G4,用100mL质量浓度为95%的乙醇洗涤颗粒物质G4,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H4;将颗粒物质H4加入到溶液B5中,并在摇床中摇动3h,过滤除去液体得到颗粒物质G5,用100mL质量浓度为95%的乙醇洗涤颗粒物质G5,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质H5;将H5置于马弗炉中在580℃条件下焙烧4h,得到颗粒物质I。Add granular substance F to solution B1, shake it in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G1, wash granular substance G1 with 100 mL of ethanol with a mass concentration of 95%, repeat the washing 2 times, and then place it at 80°C Dry at 95°C for 10 hours to obtain granular substance H1 ; add granular substance H1 to solution B2 , and shake in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G2, and wash the granular substance with 100 mL of ethanol with a mass concentration of 95% G2, repeat washing twice, and then dry at 80°C for 10 hours to obtain granular substance H2 ; add granular substance H2 to solution B3 , shake it in a shaker for 3 hours, filter and remove the liquid to obtain granular substance G3, Wash the granular substance G3 with 100mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then dry it at 80°C for 10h to obtain the granular substance H3 ; add the granular substance H3 to the solution B4 , and shake Shake in medium for 3 hours, remove the liquid by filtration to obtain granular substance G4, wash granular substance G4 with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then dry at 80°C for 10 hours to obtain granular substance H4 ; 4 was added to solution B5 , and shaken in a shaker for 3 hours, filtered to remove the liquid to obtain granular substance G5, washed with 100mL of ethanol with a mass concentration of 95%, repeated washing twice, and then dried at 80°C After 10 hours, granular substance H 5 was obtained; H 5 was calcined in a muffle furnace at 580° C. for 4 hours to obtain granular substance I.
将20ml浓度为0.5mol/L的Ce(NO3)2溶液和80ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入20ml浓度为0.5mol/L的MnCl2溶液,得到溶液C。Add 20ml of Ce(NO 3 ) solution with a concentration of 0.5mol/L and 80ml of CuCl solution with a concentration of 0.5mol/L into 120ml of isopropanol and 5ml of concentrated hydrochloric acid, and then add 20ml of a solution with a concentration of 0.5mol/L MnCl 2 solution to obtain solution C.
将颗粒物质I加入到溶液C中,并在摇床中摇动3h;过滤除去液体得到颗粒物质J,用100mL质量浓度为95%的乙醇洗涤颗粒物质J,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质K。Add granular substance I to solution C, and shake it in a shaker for 3 hours; filter and remove the liquid to obtain granular substance J, wash granular substance J with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then store the granular substance at 80°C Under drying for 10 h, granular material K was obtained.
将40ml浓度为0.5mol/L的Ce(NO3)2溶液和40ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入40ml浓度为0.5mol/L的MnCl2溶液,得到溶液D。Add 40ml of Ce(NO 3 ) solution with a concentration of 0.5mol/L and 40ml of CuCl solution with a concentration of 0.5mol/L into 120ml of isopropanol and 5ml of concentrated hydrochloric acid, and then add 40ml of a concentration of 0.5mol/L with MnCl 2 solution to obtain solution D.
将颗粒物质K加入到溶液D中,并在摇床中摇动3h;过滤除去液体得到颗粒物质L,用100mL质量浓度为95%的乙醇洗涤颗粒物质L,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质M。Add granular substance K to solution D, and shake it in a shaker for 3 hours; filter and remove the liquid to obtain granular substance L, wash granular substance L with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then store it at 80°C Under drying for 10h, the granular material M was obtained.
将45ml浓度为0.5mol/L的Ce(NO3)2溶液和15ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入60ml浓度为0.5mol/L的MnCl2溶液,得到溶液E。Add 45ml of Ce(NO 3 ) 2 solution with a concentration of 0.5mol/L and 15ml of CuCl 2 solution with a concentration of 0.5mol/L into 120ml of isopropanol and 5ml of concentrated hydrochloric acid, and then add 60ml of 0.5mol/L with a concentration of MnCl 2 solution to obtain solution E.
将颗粒物质M加入到溶液E中,并在摇床中摇动3h;过滤除去液体得到颗粒物质N,用100mL质量浓度为95%的乙醇洗涤颗粒物质N,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质O。Add the particulate matter M to the solution E, and shake it in a shaker for 3 hours; remove the liquid by filtration to obtain the particulate matter N, wash the granular matter N with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then store it at 80°C Under drying for 10h, granular material O was obtained.
将15ml浓度为0.5mol/L的Ce(NO3)2溶液和5ml浓度为0.5mol/L的CuCl2溶液加入到120ml异丙醇和5ml浓盐酸中,然后再加入100ml浓度为0.5mol/L的MnCl2溶液,得到溶液F。Add 15ml of Ce(NO 3 ) 2 solution with a concentration of 0.5mol/L and 5ml of CuCl 2 solution with a concentration of 0.5mol/L into 120ml of isopropanol and 5ml of concentrated hydrochloric acid, and then add 100ml of 0.5mol/L MnCl 2 solution to obtain solution F.
将颗粒物质O加入到溶液F中,并在摇床中摇动3h;过滤除去液体得到颗粒物质P,用100mL质量浓度为95%的乙醇洗涤颗粒物质P,重复洗涤2次,然后在80℃条件下干燥10h,得到颗粒物质Q,将Q置于马弗炉中在580℃条件下焙烧4h,得到的颗粒物质即为含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极。Add the particulate matter O to the solution F and shake it in a shaker for 3 hours; remove the liquid by filtration to obtain the particulate matter P, wash the particulate matter P with 100 mL of ethanol with a mass concentration of 95%, repeat the washing twice, and then store it at 80°C Drying for 10 hours under the hood to obtain granular material Q, put Q in a muffle furnace and bake at 580°C for 4 hours, and the obtained granular material is the Ag-doped MnO 2 -CeO 2 activated alumina particle electrode containing CuO interlayer .
下面是运用本发明方法制得的含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极在三维电极反应器中对煤化工废水进行了降解试验,进一步说明本发明。In the following, the Ag-doped MnO 2 -CeO 2 active alumina particle electrode containing a CuO intermediate layer prepared by the method of the present invention was used to conduct a degradation test on coal chemical industry wastewater in a three-dimensional electrode reactor to further illustrate the present invention.
将本发明方法制得的含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子电极装填在三维电极反应器中,对煤化工废水进行了降解试验,结果表明该电极能够高效处理焦化废水中的COD,当进水COD为512mg/L时,以含CuO中间层的负载Ag掺杂MnO2-CeO2活性氧化铝粒子为第三极,pH为4.5,电压为12V,处理时间为60min,处理后出水中的COD降低到44mg/L,处理效率达到91.41%。The Ag-doped MnO 2 -CeO 2 activated alumina particle electrode containing the CuO intermediate layer prepared by the method of the present invention is packed in a three-dimensional electrode reactor, and a degradation test is carried out on coal chemical industry wastewater, and the results show that the electrode can be efficiently treated For COD in coking wastewater, when the influent COD is 512mg/L, the Ag-doped MnO 2 -CeO 2 activated alumina particles containing the CuO intermediate layer are used as the third pole, the pH is 4.5, the voltage is 12V, and the treatment time After 60 minutes, the COD in the effluent after treatment was reduced to 44mg/L, and the treatment efficiency reached 91.41%.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310525735.1A CN103539227B (en) | 2013-10-30 | 2013-10-30 | Preparation Technology of Ag-doped MnO2-CeO2 Active Alumina Particle Electrode Containing CuO Interlayer |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201310525735.1A CN103539227B (en) | 2013-10-30 | 2013-10-30 | Preparation Technology of Ag-doped MnO2-CeO2 Active Alumina Particle Electrode Containing CuO Interlayer |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103539227A true CN103539227A (en) | 2014-01-29 |
CN103539227B CN103539227B (en) | 2015-02-04 |
Family
ID=49963149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201310525735.1A Expired - Fee Related CN103539227B (en) | 2013-10-30 | 2013-10-30 | Preparation Technology of Ag-doped MnO2-CeO2 Active Alumina Particle Electrode Containing CuO Interlayer |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103539227B (en) |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106495285A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified nickel foam granule electrode and the preparation method of pyridine functional |
CN106495279A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified nickel foam granule electrode and the preparation method of chlorophenol function |
CN106495287A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified carbon fiber granule electrode and the preparation method of chlorophenol function |
CN106495280A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove improved ferroferric oxide granule electrode and the preparation method of phenol function |
CN106495283A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove Modified Activated Carbon aerogel particles electrode and the preparation method of phenol function |
CN106495286A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified titanium foam granule electrode and the preparation method of benzoquinone function |
CN106495281A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified activated carbon granule electrode and the preparation method of carbazole function |
CN106495290A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified graphite granule electrode and the preparation method of benzoquinone function |
CN106495282A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified activated carbon granule electrode and the preparation method of benzoquinones function |
CN106495278A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified titanium foam granule electrode and the preparation method of phenol function |
CN106495288A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified quartz particles electrode and the preparation method of chlorophenol function |
CN106517431A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified ceramic particle electrode with electrocatalytic carbazole removing function and preparing method thereof |
CN106517434A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified activated carbon particle electrode with function of removing pyridine through electro-catalysis, and preparation method of modified activated carbon particle electrode |
CN106517444A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified zeolite particle electrode capable of realizing electrocatalytic removal of indole and preparation method thereof |
CN106517429A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified ceramic particle electrode with function of removing furan through electro-catalysis and preparation method |
CN108083393A (en) * | 2017-12-28 | 2018-05-29 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on PbO-NiO-MgO and thiophene |
CN108163931A (en) * | 2017-12-28 | 2018-06-15 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on CeO-ZrO-NiO and pyrazine |
CN108178247A (en) * | 2017-12-28 | 2018-06-19 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on CrO-FeO-PbO and quinoline |
CN108178248A (en) * | 2017-12-28 | 2018-06-19 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on CuO-CoO-ZnO and pyridine |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2461023A1 (en) * | 1979-07-02 | 1981-01-30 | Olin Corp | PROCESS FOR PREPARING CONDUCTIVE SUBSTRATES AND ELECTRODES FOR THE ELECTROLYSIS OF A BRINE, AND THE LOW-VOLTAGE ELECTRODE THUS OBTAINED |
EP1160357A1 (en) * | 2000-05-30 | 2001-12-05 | Creavis Gesellschaft für Technologie und Innovation mbH | Electrochemical cell for the oxidation of organic compounds and electrocatalytic oxidation process |
WO2002094418A1 (en) * | 2001-05-22 | 2002-11-28 | Dinex A/S | Method and apparatus for electrochemical reduction of nitrogen oxides in a mixture of nitrogen oxides and oxygen |
CN101736369A (en) * | 2009-12-29 | 2010-06-16 | 昆明理工大学 | Method for preparing novel aluminum-based composite lead dioxide-manganese dioxide anode for zinc electrodeposition |
CN102225797A (en) * | 2011-04-20 | 2011-10-26 | 上海电力学院 | A rare earth element-doped titanium-based manganese dioxide electrode and its preparation method |
-
2013
- 2013-10-30 CN CN201310525735.1A patent/CN103539227B/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2461023A1 (en) * | 1979-07-02 | 1981-01-30 | Olin Corp | PROCESS FOR PREPARING CONDUCTIVE SUBSTRATES AND ELECTRODES FOR THE ELECTROLYSIS OF A BRINE, AND THE LOW-VOLTAGE ELECTRODE THUS OBTAINED |
EP1160357A1 (en) * | 2000-05-30 | 2001-12-05 | Creavis Gesellschaft für Technologie und Innovation mbH | Electrochemical cell for the oxidation of organic compounds and electrocatalytic oxidation process |
WO2002094418A1 (en) * | 2001-05-22 | 2002-11-28 | Dinex A/S | Method and apparatus for electrochemical reduction of nitrogen oxides in a mixture of nitrogen oxides and oxygen |
CN101736369A (en) * | 2009-12-29 | 2010-06-16 | 昆明理工大学 | Method for preparing novel aluminum-based composite lead dioxide-manganese dioxide anode for zinc electrodeposition |
CN102225797A (en) * | 2011-04-20 | 2011-10-26 | 上海电力学院 | A rare earth element-doped titanium-based manganese dioxide electrode and its preparation method |
Cited By (19)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106495285A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified nickel foam granule electrode and the preparation method of pyridine functional |
CN106495279A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified nickel foam granule electrode and the preparation method of chlorophenol function |
CN106495287A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified carbon fiber granule electrode and the preparation method of chlorophenol function |
CN106495280A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove improved ferroferric oxide granule electrode and the preparation method of phenol function |
CN106495283A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove Modified Activated Carbon aerogel particles electrode and the preparation method of phenol function |
CN106495286A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified titanium foam granule electrode and the preparation method of benzoquinone function |
CN106495281A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified activated carbon granule electrode and the preparation method of carbazole function |
CN106495290A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified graphite granule electrode and the preparation method of benzoquinone function |
CN106495282A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified activated carbon granule electrode and the preparation method of benzoquinones function |
CN106495278A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified titanium foam granule electrode and the preparation method of phenol function |
CN106495288A (en) * | 2016-11-21 | 2017-03-15 | 北京益清源环保科技有限公司 | There is electro-catalysis to remove modified quartz particles electrode and the preparation method of chlorophenol function |
CN106517431A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified ceramic particle electrode with electrocatalytic carbazole removing function and preparing method thereof |
CN106517434A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified activated carbon particle electrode with function of removing pyridine through electro-catalysis, and preparation method of modified activated carbon particle electrode |
CN106517444A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified zeolite particle electrode capable of realizing electrocatalytic removal of indole and preparation method thereof |
CN106517429A (en) * | 2016-11-21 | 2017-03-22 | 北京益清源环保科技有限公司 | Modified ceramic particle electrode with function of removing furan through electro-catalysis and preparation method |
CN108083393A (en) * | 2017-12-28 | 2018-05-29 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on PbO-NiO-MgO and thiophene |
CN108163931A (en) * | 2017-12-28 | 2018-06-15 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on CeO-ZrO-NiO and pyrazine |
CN108178247A (en) * | 2017-12-28 | 2018-06-19 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on CrO-FeO-PbO and quinoline |
CN108178248A (en) * | 2017-12-28 | 2018-06-19 | 光合强化(北京)生物科技有限公司 | The graphite electrode modified based on CuO-CoO-ZnO and pyridine |
Also Published As
Publication number | Publication date |
---|---|
CN103539227B (en) | 2015-02-04 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103539227B (en) | Preparation Technology of Ag-doped MnO2-CeO2 Active Alumina Particle Electrode Containing CuO Interlayer | |
CN103539229B (en) | Particle electrode for efficiently removing various organic compounds and preparation method thereof | |
CN104925913B (en) | For removing catalyst particle electrode of hardly degraded organic substance and ammonia nitrogen and its preparation method and application in decontamination sewage | |
CN110237818B (en) | A kind of preparation method and application of nitrogen-sulfur co-doped biochar | |
CN100429155C (en) | Particle electrode catalyst filler for three-dimensional electrode reactor and preparation method thereof | |
CN105056882A (en) | Preparation method of modified charcoal-based adsorbent for removing hydrogen sulfide | |
CN110773166B (en) | Preparation method and application of biomass carbon-based bimetallic catalyst for water treatment | |
CN103663631A (en) | Three-dimensional particle electrode loaded with catalyst active carbon and preparation method thereof | |
CN104549155A (en) | Biological activated carbon composite material and application thereof | |
CN105668719B (en) | Cobalt oxide loaded active carbon catalytic particle electrode and preparation method thereof | |
CN107413835B (en) | Method for restoring petroleum polluted soil | |
CN106914216A (en) | A kind of preparation of feces of livestock and poultry charcoal and its method for removing sulfa antibiotics in water removal | |
CN110898802B (en) | Sludge-based biochar, preparation method and application thereof, acetic acid-modified sludge-based biochar, preparation method and application thereof | |
CN103981537B (en) | The preparation method of the Pd/3DOM TiO2/BDD electrode of a kind of photoelectrocatalysis reduction treatment organic pollution and application thereof | |
CN106064962A (en) | Utilize mud and coal ash for manufacturing for the method for catalyst particle electrode and application | |
CN104016449A (en) | Preparation and application of a Sb-Ni-Nd co-doped SnO2 high catalytic activity anode | |
CN103553188B (en) | Electrocatalytic particle electrode material for treating high-concentration organic wastewater and preparation process thereof | |
CN103551164B (en) | Nitrogenous sulphur oxygen helerocyclics is had to eelctro-catalyst and the preparation method of efficient catalytic degradation function | |
CN103041775B (en) | Graphene oxidation reactor based on graphene macro-body and application of graphene oxidation reactor | |
CN106179215A (en) | The preparation method of water plant charcoal carbon nano tube compound material and application | |
CN107377608A (en) | It is a kind of efficiently to remove Cr in acid soil6+Microbial fuel cell unit and method | |
CN110038544A (en) | A kind of nano-carbon material and preparation method thereof for heterogeneous Fenton's reaction | |
CN106587277A (en) | Carbon black-nanometer iron oxide/polytetrafluoroethylene heterogeneous tubular membrane electrode | |
CN114452967A (en) | An acetic acid and ball-milling modified sludge biochar for efficient degradation of imidacloprid in water by synergistic electrochemical activation of peroxymonosulfate | |
CN103086459B (en) | Method for removing humic acid in water by magnetic nanometer carbon and regeneration method of magnetic nanometer carbon |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150204 Termination date: 20151030 |
|
EXPY | Termination of patent right or utility model |