WO2016074400A1 - Carbon-supported catalyst and manufacturing method therefor - Google Patents
Carbon-supported catalyst and manufacturing method therefor Download PDFInfo
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- WO2016074400A1 WO2016074400A1 PCT/CN2015/074427 CN2015074427W WO2016074400A1 WO 2016074400 A1 WO2016074400 A1 WO 2016074400A1 CN 2015074427 W CN2015074427 W CN 2015074427W WO 2016074400 A1 WO2016074400 A1 WO 2016074400A1
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- WIPO (PCT)
- Prior art keywords
- carbon
- supported
- catalyst
- oxide catalyst
- activated carbon
- Prior art date
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 157
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 8
- 239000004744 fabric Substances 0.000 claims abstract description 22
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 116
- NDVLTYZPCACLMA-UHFFFAOYSA-N silver oxide Chemical compound [O-2].[Ag+].[Ag+] NDVLTYZPCACLMA-UHFFFAOYSA-N 0.000 claims description 56
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 42
- MUMZUERVLWJKNR-UHFFFAOYSA-N oxoplatinum Chemical compound [Pt]=O MUMZUERVLWJKNR-UHFFFAOYSA-N 0.000 claims description 28
- 229910003446 platinum oxide Inorganic materials 0.000 claims description 28
- 229910001923 silver oxide Inorganic materials 0.000 claims description 28
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 claims description 27
- 239000005751 Copper oxide Substances 0.000 claims description 27
- 229910000431 copper oxide Inorganic materials 0.000 claims description 27
- 241000209094 Oryza Species 0.000 claims description 20
- 235000007164 Oryza sativa Nutrition 0.000 claims description 20
- 235000009566 rice Nutrition 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 16
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 claims description 14
- 238000001035 drying Methods 0.000 claims description 13
- 229910052799 carbon Inorganic materials 0.000 claims description 12
- 229910044991 metal oxide Inorganic materials 0.000 claims description 12
- 150000004706 metal oxides Chemical class 0.000 claims description 12
- 238000001816 cooling Methods 0.000 claims description 9
- 239000011521 glass Substances 0.000 claims description 9
- 229910001220 stainless steel Inorganic materials 0.000 claims description 9
- 239000010935 stainless steel Substances 0.000 claims description 9
- 238000003756 stirring Methods 0.000 claims description 8
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical compound [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 claims description 7
- 239000003292 glue Substances 0.000 claims description 7
- NWAHZABTSDUXMJ-UHFFFAOYSA-N platinum(2+);dinitrate Chemical compound [Pt+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O NWAHZABTSDUXMJ-UHFFFAOYSA-N 0.000 claims description 7
- 229910001961 silver nitrate Inorganic materials 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 239000004745 nonwoven fabric Substances 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 2
- 229910052738 indium Inorganic materials 0.000 claims 1
- 238000002525 ultrasonication Methods 0.000 claims 1
- 230000003197 catalytic effect Effects 0.000 abstract description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 2
- 230000002035 prolonged effect Effects 0.000 abstract 1
- 230000036647 reaction Effects 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 49
- 238000001132 ultrasonic dispersion Methods 0.000 description 7
- 238000002360 preparation method Methods 0.000 description 5
- 238000005979 thermal decomposition reaction Methods 0.000 description 4
- 108010010803 Gelatin Proteins 0.000 description 3
- 239000011247 coating layer Substances 0.000 description 3
- 239000008273 gelatin Substances 0.000 description 3
- 229920000159 gelatin Polymers 0.000 description 3
- 235000019322 gelatine Nutrition 0.000 description 3
- 235000011852 gelatine desserts Nutrition 0.000 description 3
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000499 gel Substances 0.000 description 2
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9016—Oxides, hydroxides or oxygenated metallic salts
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/88—Processes of manufacture
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
-
- H—ELECTRICITY
- H01—ELECTRIC ELEMENTS
- H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
- H01M4/00—Electrodes
- H01M4/86—Inert electrodes with catalytic activity, e.g. for fuel cells
- H01M4/90—Selection of catalytic material
- H01M4/9075—Catalytic material supported on carriers, e.g. powder carriers
- H01M4/9083—Catalytic material supported on carriers, e.g. powder carriers on carbon or graphite
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/50—Fuel cells
Definitions
- the present invention relates to a catalyst, and more particularly to a carbon supported catalyst and a method of making the same.
- An object of the present invention is to provide a carbon-supported catalyst which has the effect of being waterproof and gas permeable, can maintain the properties of the carbon-supported catalyst, and is not easily decomposed.
- a carbon-supported catalyst comprising a cloth layer, a coating layer disposed on the cloth layer, and a waterproof gas permeable layer on the catalyst layer.
- the composition ratio of the catalyst layer is: mass ratio of carbon-supported copper oxide 80-120g, carbon-supported silver oxide catalyst 0.4-0.6g, carbon-supported platinum oxide catalyst 0.2-0.3g, glutinous rice glue 4 -6g.
- the mass ratio of each of the three metal oxides to the activated carbon is 3:80-120.
- the composition of the waterproof gas permeable layer is in a mass ratio of 8-12 g of glutinous rice gum and 20 g of activated carbon 80-1.
- the method for preparing the carbon-supported catalyst comprises the following steps:
- a carbon-supported metal oxide catalyst comprising a carbon-supported copper oxide catalyst, a carbon-supported silver oxide catalyst and a carbon-supported platinum oxide catalyst
- step A preparing the carbon-supported copper oxide catalyst ⁇ comprises the following steps:
- preparing the carbon-supported silver oxide catalyst ⁇ comprises the following steps:
- preparing the carbon-supported platinum oxide catalyst ⁇ comprises the following steps:
- the dried material is wrapped with a glass cloth, placed in a stainless steel box, baked at 450 ° C, held for 1 hour, thermal decomposition of platinum nitrate to produce platinum oxide, waiting for natural cooling, obtained with activated carbon as a carrier Platinum oxide catalyst.
- the step B includes the following steps:
- the step C comprises: preparing 8-12 g of glutinous rice gel into a viscous state, adding 80-120 g of activated carbon, mixing, adding 100 ml of ethanol, diluting and stirring uniformly, and then uniformly coating with an animal brush.
- the cloth is coated on the catalyst layer and then dried in a drying oven to obtain the waterproof gas permeable layer.
- a waterproof gas permeable layer is disposed on the catalyst layer, and the carbon-supported catalyst participates in the reaction of the battery, and the waterproof gas permeable layer can protect the catalyst, and the catalyst is not easily accommodated while ensuring the catalytic effect of the catalyst. Decomposition, greatly improving the battery life.
- Embodiment 1 A carbon-supported catalyst comprising a cloth layer, a coating layer disposed on the cloth layer, and a waterproof gas permeable layer disposed on the catalyst layer.
- the composition of the catalyst layer is as follows: mass ratio of carbon-supported copper oxide catalyst 80g, carbon-supported silver oxide catalyst 0.6g, carbon-supported platinum oxide catalyst 0.25g, glutinous rice glue 5g, composition of the waterproof gas-permeable layer by mass The ratio is: 8 g of glutinous rice gelatin and 120 g of activated carbon.
- the method for preparing the carbon-supported catalyst comprises the following steps:
- a carbon-supported metal oxide catalyst, the carbon-supported metal oxide catalyst comprises a carbon-supported copper oxide catalyst, a carbon-supported silver oxide catalyst and a carbon-supported platinum oxide catalyst to produce carbon-supported copper oxide Catalyst ⁇ , including the following steps:
- the dried product was wrapped in a glass cloth, placed in a stainless steel box, baked at 450 ° C, and kept for 1 hour to thermally decompose copper nitrate to produce copper oxide. After waiting for natural cooling, a copper oxide catalyst supported by activated carbon was obtained.
- the preparation of the carbon-supported silver oxide catalyst ⁇ includes the following steps:
- the silver nitrate solution can obtain 15g of silver oxide after thermal decomposition reaction, so that the mass ratio of silver oxide to activated carbon is maintained at 3:80-120;
- the preparation of the carbon-supported platinum oxide catalyst ⁇ includes the following steps:
- the catalyst layer is prepared, 80 prepared carbon-supported copper oxide catalyst, 0.6 g of carbon-supported silver oxide catalyst, and 0.25 g of carbon-supported platinum oxide catalyst are mixed and stirred to form a ternary oxide catalyst, 1 5 ml of ethanol was continuously stirred, 5 g of glutinous rice gum was added, and the mixture was stirred until it was viscous, and then it was applied onto a nonwoven fabric carrier, and dried by a drying oven to obtain the catalyst layer.
- the waterproof gas permeable layer was prepared, 8 g of glutinous rice glue was prepared to be viscous, and 120 g of activated carbon was added and mixed, and then diluted with 100 ml of ethanol, stirred uniformly, and then uniformly coated with the animal hair brush. Catalyst layer Above, it is then dried in a dry box to obtain the waterproof gas permeable layer, and the carbon-supported catalyst is formed.
- a carbon-supported catalyst comprising a cloth layer, a coating layer disposed on the cloth layer, and a waterproof gas permeable layer on the catalyst layer.
- the composition ratio of the catalyst layer is: 00g of carbon-supported copper oxide catalyst, 0.5g of carbon-supported silver oxide catalyst, 0.3g of carbon-supported platinum oxide catalyst, 4g of glutinous rice glue; the composition of the waterproof gas-permeable layer is The mass ratio is: 10 g of glutinous rice glue and 80 g of activated carbon.
- the method for preparing the carbon-supported catalyst comprises the following steps:
- the catalyst layer is prepared, and 100 g of the prepared carbon-supported copper oxide catalyst, 0.5 g of a carbon-supported silver oxide catalyst, and 0.3 g of a carbon-supported platinum oxide catalyst are mixed and stirred to form a ternary oxide catalyst.
- the waterproof gas permeable layer was prepared, 10 g of glutinous rice gelatin was prepared into a viscous shape, and 80 g of activated carbon was added and mixed, and then diluted with 100 ml of ethanol and uniformly stirred, followed by uniform coating with the animal hair brush.
- the catalyst layer is then dried on a drying oven to obtain the water-repellent gas permeable layer, and the carbon-supported catalyst is formed.
- a carbon-supported catalyst comprising a cloth layer, a catalyst layer disposed on the cloth layer, and a waterproof gas permeable layer disposed on the catalyst layer.
- the composition of the catalyst layer is as follows: mass ratio of carbon-supported copper oxide catalyst 20g, carbon-supported silver oxide catalyst 0.4g, carbon-supported platinum oxide catalyst 0.2g, glutinous rice gum 6g; composition of the waterproof gas-permeable layer The mass ratio is: 9 g of glutinous rice gelatin and 100 g of activated carbon.
- the method for preparing the carbon-supported catalyst comprises the following steps:
- the catalyst layer is prepared, 120 g of the prepared carbon-supported copper oxide catalyst, 0.4 g of carbon-supported silver oxide catalyst, and 0.2 g of carbon-supported platinum oxide catalyst are mixed and stirred to form a ternary oxide catalyst, 15 ml of ethanol was continuously stirred, 6 g of glutinous rice gum was added, and the mixture was stirred until it was viscous, and then it was applied onto a nonwoven fabric carrier, and dried by a drying oven to obtain the catalyst layer.
- the waterproof gas-permeable layer is prepared, and 9 g of glutinous rice glue is prepared into a viscous shape. After adding 100 g of activated carbon, the mixture is diluted with 100 ml of ethanol, stirred uniformly, and then uniformly coated on the catalyst layer with an animal brush. Then, it is dried in a dry box to obtain the waterproof gas permeable layer, and the carbon-supported catalyst is formed.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Materials Engineering (AREA)
- Manufacturing & Machinery (AREA)
- Catalysts (AREA)
Abstract
The present invention relates to a catalyst, and particularly to a carbon-supported catalyst and a manufacturing method therefor. The carbon-supported catalyst comprises a cloth layer. A catalyst layer is arranged on the cloth layer, and a waterproof breathable layer is arranged on the catalyst layer. According to the carbon-supported catalyst in the present invention, a waterproof breathable layer is arranged on a catalyst layer; and when the carbon-supported catalyst participates in a cell reaction, the waterproof breathable layer can protect the catalyst, so that the catalyst is not easy to decompose while the catalytic effect of the catalyst is guaranteed, and the service life of a cell is greatly prolonged.
Description
一种碳载催化剂及其制作方法 Carbon-supported catalyst and preparation method thereof
技术领域 Technical field
[0001] 本发明涉及一种催化剂, 尤其涉及一种碳载催化剂及其制作方法。 [0001] The present invention relates to a catalyst, and more particularly to a carbon supported catalyst and a method of making the same.
背景技术 Background technique
[0002] 传统混合型应用于燃料电池中的催化剂, 由于其催化剂层和电池中的电解液直 接接触, 在经过电池内部反应后容易出现被分解的情况, 大大影响电池的使用 寿命。 [0002] Conventional hybrid type catalysts used in fuel cells are prone to decomposition due to direct contact between the catalyst layer and the electrolyte in the battery, which greatly affects the service life of the battery.
技术问题 technical problem
[0003] 本发明的目的在于提供一种碳载催化剂, 其拥有防水透气的效果, 能保持碳载 催化剂性质稳定, 不容易被分解。 [0003] An object of the present invention is to provide a carbon-supported catalyst which has the effect of being waterproof and gas permeable, can maintain the properties of the carbon-supported catalyst, and is not easily decomposed.
问题的解决方案 Problem solution
技术解决方案 Technical solution
[0004] 为实现上述目的, 本发明采用如下技术方案: [0004] In order to achieve the above object, the present invention adopts the following technical solutions:
[0005] 一种碳载催化剂, 包括一布层, 所述布层上设有一催化剂层, 所述催化剂层上 设有一防水透气层。 [0005] A carbon-supported catalyst comprising a cloth layer, a coating layer disposed on the cloth layer, and a waterproof gas permeable layer on the catalyst layer.
[0006] 作为优选, 所述催化剂层的组成成分按质量比为: 碳载氧化铜催化剂 80-120g , 碳载氧化银催化剂 0.4-0.6g, 碳载氧化铂催化剂 0.2-0.3g, 糯米胶 4-6g。 [0006] Preferably, the composition ratio of the catalyst layer is: mass ratio of carbon-supported copper oxide 80-120g, carbon-supported silver oxide catalyst 0.4-0.6g, carbon-supported platinum oxide catalyst 0.2-0.3g, glutinous rice glue 4 -6g.
[0007] 作为优选, 所述碳载氧化铜催化剂, 碳载氧化银催化剂, 碳载氧化铂催化剂中 , 三种金属氧化物各自和活性碳的质量比都为 3:80-120。 Preferably, in the carbon supported copper oxide catalyst, the carbon supported silver oxide catalyst, and the carbon supported platinum oxide catalyst, the mass ratio of each of the three metal oxides to the activated carbon is 3:80-120.
[0008] 作为优选, 所述防水透气层的组成成分按质量比为: 糯米胶 8-12g和活性碳 80-1 20g。 Preferably, the composition of the waterproof gas permeable layer is in a mass ratio of 8-12 g of glutinous rice gum and 20 g of activated carbon 80-1.
[0009] 所述碳载催化剂的制作方法, 包括以下步骤: [0009] The method for preparing the carbon-supported catalyst comprises the following steps:
[0010] A . 制作碳载金属氧化物催化剂, 所述碳载金属氧化物催化剂包括碳载氧化铜 催化剂, 碳载氧化银催化剂和碳载氧化铂催化剂; [0010] A carbon-supported metal oxide catalyst comprising a carbon-supported copper oxide catalyst, a carbon-supported silver oxide catalyst and a carbon-supported platinum oxide catalyst;
[0011] B . 制作所述催化剂层; [0011] B. Making the catalyst layer;
[0012] C . 制作所述防水透气层。
[0013] 作为优选, 所述步骤 A中, 制作碳载氧化铜催化剂吋, 包括以下步骤: [0012] C. The waterproof gas permeable layer is fabricated. [0013] Preferably, in the step A, preparing the carbon-supported copper oxide catalyst 吋 comprises the following steps:
[0014] a)将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; [0014] a) 400-600g of 400 mesh activated carbon was added to 100 ml of ethanol, and treated by ultrasonic dispersion;
[0015] b)将 210g质量分数为 20%的硝酸铜溶液加入处理后的活性碳中, 用搅拌器充分 搅拌, 并放置 24小吋; [0015] b) 210g of a 20% copper nitrate solution was added to the treated activated carbon, stirred thoroughly with a stirrer, and placed 24 hours;
[0016] c)将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; [0016] c) placing the activated carbon after standing in a dry box at 100 degrees Celsius until dry;
[0017] d)将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙烧, 保温 1 小吋, 使硝酸铜热分解产生氧化铜, 等待自然冷却后, 得到以活性炭为载体的 氧化铜催化剂。 [0017] d) The dried material is wrapped with a glass cloth, placed in a stainless steel box, baked at 450 ° C, and kept for 1 hour to thermally decompose copper nitrate to produce copper oxide. After waiting for natural cooling, the activated carbon is obtained as a carrier. Copper oxide catalyst.
[0018] 作为优选, 所述步骤 A中, 制作碳载氧化银催化剂吋, 包括以下步骤: [0018] Preferably, in the step A, preparing the carbon-supported silver oxide catalyst 吋 comprises the following steps:
[0019] a)将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; [0019] a) 400-600g of 400 mesh activated carbon was added to 100 ml of ethanol, and treated by ultrasonic dispersion;
[0020] b)将 110g质量分数为 20%的硝酸银溶液加入处理后的活性碳中, 用搅拌器充分 搅拌, 并放置 24小吋; [0020] b) 110g of a 20% silver nitrate solution was added to the treated activated carbon, fully stirred with a stirrer, and placed 24 hours;
[0021] c)将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; [0021] c) placing the activated carbon after standing in a dry box at 100 degrees Celsius until drying;
[0022] d)将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙烧, 保温 1 小吋, 使硝酸银热分解产生氧化银, 等待自然冷却后, 得到以活性炭为载体的 氧化银催化剂。 [0022] d) The dried product is wrapped with a glass cloth, placed in a stainless steel box, baked at 450 ° C, and kept for 1 hour to thermally decompose the silver nitrate to produce silver oxide. After waiting for natural cooling, the activated carbon is obtained as a carrier. Silver oxide catalyst.
[0023] 作为优选, 所述步骤 A中, 制作碳载氧化铂催化剂吋, 包括以下步骤: [0023] Preferably, in the step A, preparing the carbon-supported platinum oxide catalyst 吋 comprises the following steps:
[0024] a)将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; [0024] a) 400-600 g of 400 mesh activated carbon was added to 100 ml of ethanol, and treated by ultrasonic dispersion;
[0025] b)将 130g质量分数为 20%的硝酸铂溶液加入处理后的活性碳中, 用搅拌器充分 搅拌, 并放置 24小吋; [0025] b) 130g of a 20% by mass of platinum nitrate solution was added to the treated activated carbon, stirred thoroughly with a stirrer, and placed 24 hours;
[0026] 0将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; [0026] 0 placing the activated carbon after standing in a dry box at 100 degrees Celsius until drying;
[0027] d)将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙烧, 保温 1 小吋, 使硝酸铂热分解产生氧化铂, 等待自然冷却后, 得到以活性炭为载体的 氧化铂催化剂。 [0027] d) the dried material is wrapped with a glass cloth, placed in a stainless steel box, baked at 450 ° C, held for 1 hour, thermal decomposition of platinum nitrate to produce platinum oxide, waiting for natural cooling, obtained with activated carbon as a carrier Platinum oxide catalyst.
[0028] 作为优选, 所述步骤 B包括以下步骤: [0028] Preferably, the step B includes the following steps:
[0029] a)取 80-120g已经制备好的碳载氧化铜催化剂, 0.4-0.6g碳载氧化银催化剂, 以 及 0.2-0.3g碳载氧化铂催化剂混合搅拌, 组成三元氧化物催化剂, 加入 15毫升乙 醇, 不断搅拌, 加入 4-6g糯米胶, 搅拌至粘稠状;
[0030] b)将粘稠后的三元氧化物催化剂涂布到无纺布载体上, 利用干燥箱干燥后, 得 到所述催化剂层。 [0029] a) taking 80-120g of the prepared carbon-supported copper oxide catalyst, 0.4-0.6g of carbon-supported silver oxide catalyst, and 0.2-0.3g of carbon-supported platinum oxide catalyst mixed and stirred to form a ternary oxide catalyst, added 15 ml of ethanol, stirring constantly, adding 4-6 g of glutinous rice gel, stirring until viscous; [0030] b) Applying the viscous ternary oxide catalyst to a nonwoven fabric carrier and drying it in a drying oven to obtain the catalyst layer.
[0031] 作为优选, 所述步骤 C包括: 将 8-12g糯米胶调制到粘稠状, 加入 80-120g活性 碳混合后, 再加入 100毫升乙醇稀释后搅拌均匀, 接着用动物毛刷均匀涂布在所 述催化剂层上面, 然后用干燥箱干燥, 得到所述防水透气层。 [0031] Preferably, the step C comprises: preparing 8-12 g of glutinous rice gel into a viscous state, adding 80-120 g of activated carbon, mixing, adding 100 ml of ethanol, diluting and stirring uniformly, and then uniformly coating with an animal brush. The cloth is coated on the catalyst layer and then dried in a drying oven to obtain the waterproof gas permeable layer.
发明的有益效果 Advantageous effects of the invention
有益效果 Beneficial effect
[0032] 本发明中的碳载催化剂, 在催化剂层上设有防水透气层, 本碳载催化剂在参与 电池反应吋, 防水透气层能保护催化剂, 在保证催化剂催化效果的同吋, 不容 易被分解, 大大提高了电池的使用寿命。 [0032] In the carbon-supported catalyst of the present invention, a waterproof gas permeable layer is disposed on the catalyst layer, and the carbon-supported catalyst participates in the reaction of the battery, and the waterproof gas permeable layer can protect the catalyst, and the catalyst is not easily accommodated while ensuring the catalytic effect of the catalyst. Decomposition, greatly improving the battery life.
本发明的实施方式 Embodiments of the invention
[0033] 下面对本发明的技术方案的具体实施方式作进一步具体的说明。 [0033] Specific embodiments of the technical solutions of the present invention are further described in detail below.
[0034] 实施例 1 : 一种碳载催化剂, 包括一布层, 所述布层上设有一催化剂层, 所述 催化剂层上设有一防水透气层。 所述催化剂层的组成成分按质量比为: 碳载氧 化铜催化剂 80g, 碳载氧化银催化剂 0.6g, 碳载氧化铂催化剂 0.25g, 糯米胶 5克 , 所述防水透气层的组成成分按质量比为: 糯米胶 8g和活性碳 120g。 [0034] Embodiment 1 A carbon-supported catalyst comprising a cloth layer, a coating layer disposed on the cloth layer, and a waterproof gas permeable layer disposed on the catalyst layer. The composition of the catalyst layer is as follows: mass ratio of carbon-supported copper oxide catalyst 80g, carbon-supported silver oxide catalyst 0.6g, carbon-supported platinum oxide catalyst 0.25g, glutinous rice glue 5g, composition of the waterproof gas-permeable layer by mass The ratio is: 8 g of glutinous rice gelatin and 120 g of activated carbon.
[0035] 所述碳载催化剂的制作方法, 包括以下步骤: [0035] The method for preparing the carbon-supported catalyst comprises the following steps:
[0036] A.制作碳载金属氧化物催化剂, 所述碳载金属氧化物催化剂包括碳载氧化铜催 [0037] 化剂, 碳载氧化银催化剂和碳载氧化铂催化剂, 制作碳载氧化铜催化剂吋, 包 括以下步骤: [0036] A carbon-supported metal oxide catalyst, the carbon-supported metal oxide catalyst comprises a carbon-supported copper oxide catalyst, a carbon-supported silver oxide catalyst and a carbon-supported platinum oxide catalyst to produce carbon-supported copper oxide Catalyst 吋, including the following steps:
[0038] a) 将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; 超声波 分散处理可以让乙醇充分负载到活性炭里面; [0038] a) 400-600 g of 400 mesh activated carbon is added to 100 ml of ethanol and treated by ultrasonic dispersion; ultrasonic dispersion treatment allows ethanol to be fully loaded into the activated carbon;
[0039] b) 将 210g质量分数为 20%的硝酸铜溶液加入处理后的活性碳中, 用搅拌器充分 搅拌, 并放置 24小吋。 所述硝酸铜溶液在经过热分解反应后, 能得到 15g氧化铜[0039] b) 210 g of a 20% by mass copper nitrate solution was added to the treated activated carbon, stirred well with a stirrer, and left for 24 hours. The copper nitrate solution can obtain 15g of copper oxide after undergoing thermal decomposition reaction.
, 使氧化铜与活性碳的质量比保持在 3:80-120; , maintaining the mass ratio of copper oxide to activated carbon at 3:80-120;
[0040] 0 将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥。 乙醇能快 速的挥发水分, 使干燥过程更迅速;
[0041] d) [0040] 0 The activated carbon after standing was placed in a dry box and treated at 100 degrees Celsius until dry. Ethanol can quickly evaporate water, making the drying process more rapid; [0041] d)
将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙烧, 保温 1小 吋, 使硝酸铜热分解产生氧化铜, 等待自然冷却后, 得到以活性炭为载体的氧 化铜催化剂。 The dried product was wrapped in a glass cloth, placed in a stainless steel box, baked at 450 ° C, and kept for 1 hour to thermally decompose copper nitrate to produce copper oxide. After waiting for natural cooling, a copper oxide catalyst supported by activated carbon was obtained.
[0042] 制作碳载氧化银催化剂吋, 包括以下步骤: [0042] The preparation of the carbon-supported silver oxide catalyst 吋 includes the following steps:
[0043] a) 将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; [0043] a) 400-600 g of 400 mesh activated carbon was added to 100 ml of ethanol and treated by ultrasonic dispersion;
[0044] b) 将 110g质量分数为 20%的硝酸银溶液加入处理后的活性碳中, 用搅拌器充 分搅拌, 并放置 24小吋。 所述硝酸银溶液在经过热分解反应后, 能得到 15g氧化 银, 使氧化银与活性碳的质量比保持在 3:80-120; [0044] b) 110 g of a silver nitrate solution having a mass fraction of 20% was added to the treated activated carbon, stirred thoroughly with a stirrer, and left for 24 hours. The silver nitrate solution can obtain 15g of silver oxide after thermal decomposition reaction, so that the mass ratio of silver oxide to activated carbon is maintained at 3:80-120;
[0045] 0 将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥。 [0045] 0 The activated carbon after standing was placed in a dry box and treated at 100 ° C until dry.
[0046] d) 将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙烧, 保 温 1小吋, 使硝酸银热分解产生氧化银, 等待自然冷却后, 得到以活性炭为载体 的氧化银催化剂。 [0046] d) The dried product is wrapped with a glass cloth, placed in a stainless steel box, baked at 450 degrees Celsius, and kept for 1 hour to thermally decompose the silver nitrate to produce silver oxide. After waiting for natural cooling, the activated carbon is obtained as a carrier. Silver oxide catalyst.
[0047] 制作碳载氧化铂催化剂吋, 包括以下步骤: [0047] The preparation of the carbon-supported platinum oxide catalyst 吋 includes the following steps:
[0048] a) 将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; [0048] a) 400-600 g of 400 mesh activated carbon was added to 100 ml of ethanol and treated by ultrasonic dispersion;
[0049] b) 将 130g质量分数为 20%的硝酸铂溶液加入处理后的活性碳中, 用搅拌器充 分搅拌, 并放置 24小吋。 所述硝酸铂溶液在经过热分解反应后, 能得到 15g氧化 铂, 使氧化铂与活性碳的质量比保持在 3:80-120; [0049] b) 130 g of a 20% by mass platinum nitrate solution was added to the treated activated carbon, stirred thoroughly with a stirrer, and left for 24 hours. The platinum nitrate solution can obtain 15g of platinum oxide after thermal decomposition reaction, so that the mass ratio of platinum oxide to activated carbon is maintained at 3:80-120;
[0050] 0 将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; [0050] 0 placing the activated carbon after standing in a dry box at 100 degrees Celsius until drying;
[0051] d) 将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙烧, 保 温 1小吋, 使硝酸铂热分解产生氧化铂, 等待自然冷却后, 得到以活性炭为载体 的氧化铂催化剂。 [0051] d) The dried product is wrapped with a glass cloth, placed in a stainless steel box, baked at 450 ° C, and kept for 1 hour, to thermally decompose platinum nitrate to produce platinum oxide, and wait for natural cooling to obtain activated carbon as a carrier. Platinum oxide catalyst.
[0052] B.制作所述催化剂层, 取 80已经制备好的碳载氧化铜催化剂, 0.6g碳载氧化银 催化剂, 以及 0.25g碳载氧化铂催化剂混合搅拌, 组成三元氧化物催化剂, 加入 1 5毫升乙醇, 不断搅拌, 加入 5g糯米胶, 搅拌至粘稠状, 然后将其涂布到无纺布 载体上, 利用干燥箱干燥后, 得到所述催化剂层。 [0052] B. The catalyst layer is prepared, 80 prepared carbon-supported copper oxide catalyst, 0.6 g of carbon-supported silver oxide catalyst, and 0.25 g of carbon-supported platinum oxide catalyst are mixed and stirred to form a ternary oxide catalyst, 1 5 ml of ethanol was continuously stirred, 5 g of glutinous rice gum was added, and the mixture was stirred until it was viscous, and then it was applied onto a nonwoven fabric carrier, and dried by a drying oven to obtain the catalyst layer.
[0053] C.制作所述防水透气层, 将 8g糯米胶调制到粘稠状, 加入 120g活性碳混合后, 再加入 100毫升乙醇稀释后搅拌均匀, 接着用动物毛刷均匀涂布在所述催化剂层
上面, 然后用干燥箱干燥, 得到所述防水透气层, 并形成所述碳载催化剂。 [0053] C. The waterproof gas permeable layer was prepared, 8 g of glutinous rice glue was prepared to be viscous, and 120 g of activated carbon was added and mixed, and then diluted with 100 ml of ethanol, stirred uniformly, and then uniformly coated with the animal hair brush. Catalyst layer Above, it is then dried in a dry box to obtain the waterproof gas permeable layer, and the carbon-supported catalyst is formed.
[0054] 实施例 2: Example 2:
[0055] 一种碳载催化剂, 包括一布层, 所述布层上设有一催化剂层, 所述催化剂层上 设有一防水透气层。 所述催化剂层的组成成分按质量比为: 碳载氧化铜催化剂 1 00g, 碳载氧化银催化剂 0.5g, 碳载氧化铂催化剂 0.3g, 糯米胶 4克; 所述防水透 气层的组成成分按质量比为: 糯米胶 10g和活性碳 80g。 [0055] A carbon-supported catalyst comprising a cloth layer, a coating layer disposed on the cloth layer, and a waterproof gas permeable layer on the catalyst layer. The composition ratio of the catalyst layer is: 00g of carbon-supported copper oxide catalyst, 0.5g of carbon-supported silver oxide catalyst, 0.3g of carbon-supported platinum oxide catalyst, 4g of glutinous rice glue; the composition of the waterproof gas-permeable layer is The mass ratio is: 10 g of glutinous rice glue and 80 g of activated carbon.
[0056] 所述碳载催化剂的制作方法, 包括以下步骤: [0056] The method for preparing the carbon-supported catalyst comprises the following steps:
[0057] A. 制作碳载金属氧化物催化剂, 所述碳载金属氧化物催化剂包括碳载 [0057] A. Making a carbon-supported metal oxide catalyst, the carbon-supported metal oxide catalyst comprising carbon
[0058] 氧化铜催化剂, 碳载氧化银催化剂和碳载氧化铂催化剂, 三种金属氧化物的制 作过程与实施例一所述相似, 这里不再累述。 [0058] The copper oxide catalyst, the carbon supported silver oxide catalyst and the carbon supported platinum oxide catalyst, the preparation process of the three metal oxides is similar to that described in the first embodiment, and will not be described again here.
[0059] B.制作所述催化剂层, 取 100g已经制备好的碳载氧化铜催化剂, 0.5g碳载氧化 银催化剂, 以及 0.3g碳载氧化铂催化剂混合搅拌, 组成三元氧化物催化剂, 加入[0059] B. The catalyst layer is prepared, and 100 g of the prepared carbon-supported copper oxide catalyst, 0.5 g of a carbon-supported silver oxide catalyst, and 0.3 g of a carbon-supported platinum oxide catalyst are mixed and stirred to form a ternary oxide catalyst.
15毫升乙醇, 不断搅拌, 加入 4g糯米胶, 搅拌至粘稠状, 然后将其涂布到无纺 布载体上, 利用干燥箱干燥后, 得到所述催化剂层。 15 ml of ethanol was continuously stirred, 4 g of glutinous rice gum was added, and the mixture was stirred until it was viscous, and then coated on a nonwoven fabric carrier, and dried by a drying oven to obtain the catalyst layer.
[0060] C.制作所述防水透气层, 将 10g糯米胶调制到粘稠状, 加入 80g活性碳混合后, 再加入 100毫升乙醇稀释后搅拌均匀, 接着用动物毛刷均匀涂布在所述催化剂层 上面, 然后用干燥箱干燥, 得到所述防水透气层, 并形成所述碳载催化剂。 [0060] C. The waterproof gas permeable layer was prepared, 10 g of glutinous rice gelatin was prepared into a viscous shape, and 80 g of activated carbon was added and mixed, and then diluted with 100 ml of ethanol and uniformly stirred, followed by uniform coating with the animal hair brush. The catalyst layer is then dried on a drying oven to obtain the water-repellent gas permeable layer, and the carbon-supported catalyst is formed.
[0061] 实施例 3: Example 3:
[0062] 一种碳载催化剂, 包括一布层, 所述布层上设有一催化剂层, 所述催化剂层上 设有一防水透气层。 所述催化剂层的组成成分按质量比为: 碳载氧化铜催化剂 1 20g, 碳载氧化银催化剂 0.4g, 碳载氧化铂催化剂 0.2g, 糯米胶 6克; 所述防水透 气层的组成成分按质量比为: 糯米胶 9g和活性碳 100g。 [0062] A carbon-supported catalyst comprising a cloth layer, a catalyst layer disposed on the cloth layer, and a waterproof gas permeable layer disposed on the catalyst layer. The composition of the catalyst layer is as follows: mass ratio of carbon-supported copper oxide catalyst 20g, carbon-supported silver oxide catalyst 0.4g, carbon-supported platinum oxide catalyst 0.2g, glutinous rice gum 6g; composition of the waterproof gas-permeable layer The mass ratio is: 9 g of glutinous rice gelatin and 100 g of activated carbon.
[0063] 所述碳载催化剂的制作方法, 包括以下步骤: [0063] The method for preparing the carbon-supported catalyst comprises the following steps:
[0064] A.制作碳载金属氧化物催化剂, 所述碳载金属氧化物催化剂包括碳 [0064] A. Making a carbon-supported metal oxide catalyst, the carbon-supporting metal oxide catalyst comprising carbon
[0065] 载氧化铜催化剂, 碳载氧化银催化剂和碳载氧化铂催化剂, 三种金属氧化物的 制作过程与实施例一中所述相似, 这里不再累述。 [0065] The copper oxide-supporting catalyst, the carbon-supported silver oxide catalyst and the carbon-supported platinum oxide catalyst, the preparation process of the three metal oxides is similar to that described in the first embodiment, and will not be described again here.
[0066] B.制作所述催化剂层, 取 120g已经制备好的碳载氧化铜催化剂, 0.4g碳载氧化 银催化剂, 以及 0.2g碳载氧化铂催化剂混合搅拌, 组成三元氧化物催化剂, 加入
15毫升乙醇, 不断搅拌, 加入 6g糯米胶, 搅拌至粘稠状, 然后将其涂布到无纺 布载体上, 利用干燥箱干燥后, 得到所述催化剂层。 [0066] B. The catalyst layer is prepared, 120 g of the prepared carbon-supported copper oxide catalyst, 0.4 g of carbon-supported silver oxide catalyst, and 0.2 g of carbon-supported platinum oxide catalyst are mixed and stirred to form a ternary oxide catalyst, 15 ml of ethanol was continuously stirred, 6 g of glutinous rice gum was added, and the mixture was stirred until it was viscous, and then it was applied onto a nonwoven fabric carrier, and dried by a drying oven to obtain the catalyst layer.
C.制作所述防水透气层, 将 9g糯米胶调制到粘稠状, 加入 100g活性碳混合后, 再加入 100毫升乙醇稀释后搅拌均匀, 接着用动物毛刷均匀涂布在所述催化剂层 上面, 然后用干燥箱干燥, 得到所述防水透气层, 并形成所述碳载催化剂。
C. The waterproof gas-permeable layer is prepared, and 9 g of glutinous rice glue is prepared into a viscous shape. After adding 100 g of activated carbon, the mixture is diluted with 100 ml of ethanol, stirred uniformly, and then uniformly coated on the catalyst layer with an animal brush. Then, it is dried in a dry box to obtain the waterproof gas permeable layer, and the carbon-supported catalyst is formed.
Claims
[权利要求 1] 一种碳载催化剂, 其特征在于, 其包括一布层, 所述布层上设有一催 化剂层, 所述催化剂层上设有一防水透气层。 [Claim 1] A carbon-supported catalyst comprising a cloth layer, a catalyst layer disposed on the cloth layer, and a waterproof gas permeable layer on the catalyst layer.
[权利要求 2] 如权利要求 1所述的一种碳载催化剂, 其特征在于, 所述催化剂层的 组成成分按质量比为: 碳载氧化铜催化剂 80-120g, 碳载氧化银催化 齐 ij0.4-0.6g, 碳载氧化铂催化剂 0.2-0.3g, 糯米胶 4-6g。 [Claim 2] A carbon-supported catalyst according to claim 1, wherein the composition of the catalyst layer is in a mass ratio: 80-120 g of a carbon-supported copper oxide catalyst, and a carbon-supported silver oxide catalyst .4-0.6g, carbon-supported platinum oxide catalyst 0.2-0.3g, glutinous rice glue 4-6g.
[权利要求 3] 如权利要求 1或 2所述的一种碳载催化剂, 其特征在于, 所述碳载氧化 铜催化剂, 碳载氧化银催化剂和碳载氧化铂催化剂中, 三种金属氧化 物各自和活性碳的质量比都 3:80-120。 [Claim 3] A carbon-supported catalyst according to claim 1 or 2, wherein the carbon-supported copper oxide catalyst, the carbon-supported silver oxide catalyst, and the carbon-supported platinum oxide catalyst, three metal oxides The mass ratio of each and activated carbon is 3:80-120.
[权利要求 4] 如权利要求 3所述的一种碳载催化剂, 其特征在于, 所述防水透气层 的组成成分按质量比为: 糯米胶 8-12g和活性碳 80-120g。 [Claim 4] A carbon-supported catalyst according to claim 3, wherein the composition of the waterproof gas-permeable layer is in a mass ratio of 8-12 g of glutinous rice gum and 80-120 g of activated carbon.
[权利要求 5] 如权利要求 1所述的一种碳载催化剂的制作方法, 其特征在于, 其包 括以下步骤: [Claim 5] A method for producing a carbon-supported catalyst according to claim 1, which comprises the steps of:
A.制作碳载金属氧化物催化剂, 所述碳载金属氧化物催化剂包括碳载 氧化铜催化剂, 碳载氧化银催化剂和碳载氧化铂催化剂; A. preparing a carbon supported metal oxide catalyst comprising a carbon supported copper oxide catalyst, a carbon supported silver oxide catalyst and a carbon supported platinum oxide catalyst;
B.制作所述催化剂层; B. fabricating the catalyst layer;
C.制作所述防水透气层。 C. Making the waterproof gas permeable layer.
[权利要求 6] 如权利要求 5所述的一种碳载催化剂的制作方法, 其特征在于, 所述 步骤 A中, 制作碳载氧化铜催化剂吋, 包括以下步骤: [Claim 6] The method for producing a carbon-supported catalyst according to claim 5, wherein in the step A, the carbon-supporting copper oxide catalyst is prepared, comprising the steps of:
a) 将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理 b) 将 210g质量分数为 20%的硝酸铜溶液加入处理后的活性碳中, 用 搅拌器充分搅拌, 并放置 24小吋; a) Add 400-600g of 400 mesh activated carbon to 100ml of ethanol, disperse by ultrasonication b) Add 210g of copper nitrate solution of 20% by mass to the treated activated carbon, stir well with a stirrer, and place 24 small Inches;
c) 将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; d) 将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下 烧, 保温 1小吋, 使硝酸铜热分解产生氧化铜, 等待自然冷却后, 得 到以活性炭为载体的氧化铜催化剂。 c) Place the activated carbon after standing in a dry box at 100 ° C until dry; d) Wrap the dried material in a glass cloth, place it in a stainless steel box, and cook at 450 ° C for 1 hour. The copper nitrate is thermally decomposed to produce copper oxide, and after waiting for natural cooling, a copper oxide catalyst supported by activated carbon is obtained.
[权利要求 7] 如权利要求 5所述的一种碳载催化剂的制作方法, 其特征在于, 所述
步骤 A中, 制作碳载氧化银催化剂吋, 包括以下步骤: a)将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; b)将 110g质量分数为 20%的硝酸银溶液加入处理后的活性碳中, 用搅 拌器充分搅拌, 并放置 24小吋; [Claim 7] A method for producing a carbon-supported catalyst according to claim 5, wherein In the step A, preparing the carbon-supported silver oxide catalyst 吋 comprises the following steps: a) adding 400-600 g of 400 mesh activated carbon to 100 ml of ethanol and dispersing with ultrasonic waves; b) adding 110 g of a silver nitrate solution having a mass fraction of 20% In the treated activated carbon, stir well with a stirrer and place it for 24 hours;
c)将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; d)将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙 烧, 保温 1小吋, 使硝酸银热分解产生氧化银, 等待自然冷却后, 得 到以活性炭为载体的氧化银催化剂。 c) Place the activated carbon after standing in a dry box at 100 ° C until dry; d) Wrap the dried material in a glass cloth, place it in a stainless steel box, bake at 450 ° C, and keep it for 1 hour. Silver nitrate is thermally decomposed to produce silver oxide, and after waiting for natural cooling, a silver oxide catalyst supported on activated carbon is obtained.
[权利要求 8] 如权利要求 5所述的一种碳载催化剂的制作方法, 其特征在于, 所述 步骤 A中, 制作碳载氧化铂催化剂吋, 包括以下步骤: [Claim 8] The method for producing a carbon-supported catalyst according to claim 5, wherein in the step A, the carbon-supporting platinum oxide catalyst is prepared, comprising the steps of:
a)将 400-600g400目活性碳加入 100毫升乙醇中, 用超声波分散处理; b)将 130g质量分数为 20%的硝酸铂溶液加入处理后的活性碳中, 用搅 拌器充分搅拌, 并放置 24小吋; a) Add 400-600g of 400 mesh activated carbon to 100ml of ethanol and disperse it by ultrasonic wave; b) Add 130g of 20% platinum nitrate solution to the treated activated carbon, stir well with a stirrer, and place 24 Xiao Yan;
c)将静置后的活性碳放置到干燥箱中在 100摄氏度下处理直到干燥; d)将干燥物用玻璃丝布包好, 放置到不锈钢盒中, 在 450摄氏度下焙 烧, 保温 1小吋, 使硝酸铂热分解产生氧化铂, 等待自然冷却后, 得 到以活性炭为载体的氧化铂催化剂。 c) Place the activated carbon after standing in a dry box at 100 ° C until dry; d) Wrap the dried material in a glass cloth, place it in a stainless steel box, bake at 450 ° C, and keep it for 1 hour. The platinum nitrate is thermally decomposed to produce platinum oxide, and after waiting for natural cooling, a platinum oxide catalyst supported by activated carbon is obtained.
[权利要求 9] 如权利要求 5所述的一种碳载催化剂的制作方法, 其特征在于, 所述 步骤 B包括以下步骤: [Claim 9] The method for fabricating a carbon-supported catalyst according to claim 5, wherein the step B comprises the following steps:
a)取 80-120g已经制备好的碳载氧化铜催化剂, 0.4-0.6g碳载氧化银催 化剂, 以及 0.2-0.3g碳载氧化铂催化剂混合搅拌, 组成三元氧化物催 化剂, 加入 15毫升乙醇, 不断搅拌, 加入 4-6g糯米胶, 搅拌至粘稠状 b)将粘稠后的三元氧化物催化剂涂布到无纺布载体上, 利用干燥箱干 燥后, 得到所述催化剂层。 a) taking 80-120 g of prepared carbon-supported copper oxide catalyst, 0.4-0.6 g of carbon-supported silver oxide catalyst, and 0.2-0.3 g of carbon-supported platinum oxide catalyst, mixing and stirring to form a ternary oxide catalyst, adding 15 ml of ethanol Stirring was continued, 4-6 g of glutinous rice gum was added, and the mixture was stirred until it was viscous. b) The viscous ternary oxide catalyst was applied onto a nonwoven fabric carrier, and dried in a drying oven to obtain the catalyst layer.
[权利要求 10] 如权利要求 5所述的一种碳载催化剂的制作方法, 其特征在于, 所述 步骤 C包括: 将 8-12g糯米胶调制到粘稠状, 加入 80-120g活性碳混合 后, 再加入 100毫升乙醇稀释后搅拌均匀, 接着用动物毛刷均匀涂布
在所述催化剂层上面, 然后用干燥箱干燥, 得到所述防水透气层, 并 形成所述碳载催化剂。
[Claim 10] The method for producing a carbon-supported catalyst according to claim 5, wherein the step C comprises: preparing 8-12 g of glutinous rice gel into a viscous state, and adding 80-120 g of activated carbon to be mixed. After that, add 100 ml of ethanol to dilute and mix well, then apply evenly with animal hair brush. Above the catalyst layer, it is then dried in a drying oven to obtain the waterproof gas permeable layer, and the carbon-supported catalyst is formed.
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