CN105839150B - A kind of material modified preparation method of platinum - Google Patents
A kind of material modified preparation method of platinum Download PDFInfo
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- CN105839150B CN105839150B CN201610259868.2A CN201610259868A CN105839150B CN 105839150 B CN105839150 B CN 105839150B CN 201610259868 A CN201610259868 A CN 201610259868A CN 105839150 B CN105839150 B CN 105839150B
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- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 title claims abstract description 68
- 239000000463 material Substances 0.000 title claims abstract description 32
- 229910052697 platinum Inorganic materials 0.000 title claims abstract description 30
- 238000002360 preparation method Methods 0.000 title claims abstract description 25
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims abstract description 136
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims abstract description 60
- 229910052759 nickel Inorganic materials 0.000 claims abstract description 53
- 239000006260 foam Substances 0.000 claims abstract description 32
- 238000000151 deposition Methods 0.000 claims abstract description 30
- 230000008021 deposition Effects 0.000 claims abstract description 30
- 238000004070 electrodeposition Methods 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 24
- 238000006722 reduction reaction Methods 0.000 claims abstract description 23
- 239000003638 chemical reducing agent Substances 0.000 claims abstract description 19
- 229910052742 iron Inorganic materials 0.000 claims abstract description 16
- 239000002253 acid Substances 0.000 claims abstract description 14
- 230000009467 reduction Effects 0.000 claims abstract description 14
- 238000005470 impregnation Methods 0.000 claims abstract description 11
- 238000007654 immersion Methods 0.000 claims abstract description 10
- 238000007598 dipping method Methods 0.000 claims abstract description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000010439 graphite Substances 0.000 claims abstract description 6
- 229910002804 graphite Inorganic materials 0.000 claims abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims abstract description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims abstract description 3
- CMHKGULXIWIGBU-UHFFFAOYSA-N [Fe].[Pt] Chemical compound [Fe].[Pt] CMHKGULXIWIGBU-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910052700 potassium Inorganic materials 0.000 claims abstract description 3
- 239000011591 potassium Substances 0.000 claims abstract description 3
- 239000007788 liquid Substances 0.000 claims abstract 3
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 12
- 229910052739 hydrogen Inorganic materials 0.000 claims description 10
- 239000001257 hydrogen Substances 0.000 claims description 10
- 230000010355 oscillation Effects 0.000 claims description 10
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims description 9
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 6
- -1 hexachloroplatinum hydrogen Chemical class 0.000 claims description 5
- PMZURENOXWZQFD-UHFFFAOYSA-L Sodium Sulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=O PMZURENOXWZQFD-UHFFFAOYSA-L 0.000 claims description 4
- SURQXAFEQWPFPV-UHFFFAOYSA-L iron(2+) sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Fe+2].[O-]S([O-])(=O)=O SURQXAFEQWPFPV-UHFFFAOYSA-L 0.000 claims description 4
- 229910052938 sodium sulfate Inorganic materials 0.000 claims description 4
- 235000011152 sodium sulphate Nutrition 0.000 claims description 4
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid group Chemical group S(O)(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 4
- 238000010306 acid treatment Methods 0.000 claims description 3
- 239000012279 sodium borohydride Substances 0.000 claims description 2
- 229910000033 sodium borohydride Inorganic materials 0.000 claims description 2
- 238000000527 sonication Methods 0.000 claims description 2
- 235000003891 ferrous sulphate Nutrition 0.000 claims 1
- 239000011790 ferrous sulphate Substances 0.000 claims 1
- 150000004688 heptahydrates Chemical class 0.000 claims 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims 1
- QFJIELFEXWAVLU-UHFFFAOYSA-H tetrachloroplatinum(2+) dichloride Chemical compound Cl[Pt](Cl)(Cl)(Cl)(Cl)Cl QFJIELFEXWAVLU-UHFFFAOYSA-H 0.000 claims 1
- 239000000758 substrate Substances 0.000 abstract description 8
- 239000007772 electrode material Substances 0.000 abstract description 6
- 238000000034 method Methods 0.000 abstract description 6
- 239000011734 sodium Substances 0.000 abstract description 5
- 230000000694 effects Effects 0.000 abstract description 4
- 229910052708 sodium Inorganic materials 0.000 abstract description 4
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 abstract 1
- 238000006197 hydroboration reaction Methods 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 33
- VEORPZCZECFIRK-UHFFFAOYSA-N 3,3',5,5'-tetrabromobisphenol A Chemical compound C=1C(Br)=C(O)C(Br)=CC=1C(C)(C)C1=CC(Br)=C(O)C(Br)=C1 VEORPZCZECFIRK-UHFFFAOYSA-N 0.000 description 14
- 239000008367 deionised water Substances 0.000 description 7
- 229910021641 deionized water Inorganic materials 0.000 description 7
- 239000011550 stock solution Substances 0.000 description 7
- 238000010586 diagram Methods 0.000 description 5
- 230000009286 beneficial effect Effects 0.000 description 4
- 230000015556 catabolic process Effects 0.000 description 4
- 238000006731 degradation reaction Methods 0.000 description 4
- 239000011159 matrix material Substances 0.000 description 4
- 239000002105 nanoparticle Substances 0.000 description 4
- 239000005416 organic matter Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000011056 performance test Methods 0.000 description 4
- 239000002904 solvent Substances 0.000 description 4
- ZOMNIUBKTOKEHS-UHFFFAOYSA-L dimercury dichloride Chemical class Cl[Hg][Hg]Cl ZOMNIUBKTOKEHS-UHFFFAOYSA-L 0.000 description 3
- 238000009713 electroplating Methods 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000157 electrochemical-induced impedance spectroscopy Methods 0.000 description 2
- 239000000598 endocrine disruptor Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229910000510 noble metal Inorganic materials 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical class N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- YPFNIPKMNMDDDB-UHFFFAOYSA-K 2-[2-[bis(carboxylatomethyl)amino]ethyl-(2-hydroxyethyl)amino]acetate;iron(3+) Chemical compound [Fe+3].OCCN(CC([O-])=O)CCN(CC([O-])=O)CC([O-])=O YPFNIPKMNMDDDB-UHFFFAOYSA-K 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical group [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000007256 debromination reaction Methods 0.000 description 1
- 238000005695 dehalogenation reaction Methods 0.000 description 1
- 238000002848 electrochemical method Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000000635 electron micrograph Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000005012 migration Effects 0.000 description 1
- 238000013508 migration Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 150000003057 platinum Chemical class 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000027756 respiratory electron transport chain Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000012209 synthetic fiber Substances 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D3/00—Electroplating: Baths therefor
- C25D3/02—Electroplating: Baths therefor from solutions
- C25D3/20—Electroplating: Baths therefor from solutions of iron
-
- 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
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C18/00—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating
- C23C18/16—Chemical coating by decomposition of either liquid compounds or solutions of the coating forming compounds, without leaving reaction products of surface material in the coating; Contact plating by reduction or substitution, e.g. electroless plating
- C23C18/31—Coating with metals
- C23C18/42—Coating with noble metals
- C23C18/44—Coating with noble metals using reducing agents
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25D—PROCESSES FOR THE ELECTROLYTIC OR ELECTROPHORETIC PRODUCTION OF COATINGS; ELECTROFORMING; APPARATUS THEREFOR
- C25D5/00—Electroplating characterised by the process; Pretreatment or after-treatment of workpieces
- C25D5/34—Pretreatment of metallic surfaces to be electroplated
- C25D5/38—Pretreatment of metallic surfaces to be electroplated of refractory metals or nickel
- C25D5/40—Nickel; Chromium
-
- 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
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- 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
- C02F2001/46152—Electrodes characterised by the shape or form
- C02F2001/46157—Perforated or foraminous electrodes
- C02F2001/46161—Porous electrodes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/36—Organic compounds containing halogen
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
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- Materials Engineering (AREA)
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- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
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- Water Supply & Treatment (AREA)
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Abstract
本发明公开了一种铂改性材料的制备方法,包括以下步骤:(1)电沉积,制备电沉积液,以石墨电极作为样机,泡沫镍基材作为阴极,进行电沉制备铁/泡沫镍电极;(2)浸渍沉积,将六氯合铂氢酸溶于水中,制备得到浸渍沉积液,然后将铁/泡沫镍电极置入浸渍沉积液中反应;(3)化学还原,称取硼氢化钠或硼氢化钾溶液溶于水中制得还原剂溶液,然后将还原剂溶液加入所述步骤(2)的浸渍沉积液中还原,得到铂‑铁/镍电极,即Pt‑Fe/Ni电极。本发明采用电沉积、浸渍沉积和化学还原法制备Pt改性电极Pt‑Fe/Ni,不但制备条件易于控制,而且Pt、Fe呈纳米形状负载于泡沫镍上,提高了原铂电极材料的表面积,促进了电极的电催化活性。
The invention discloses a method for preparing a platinum modified material, which comprises the following steps: (1) Electrodeposition, preparing an electrodeposition liquid, using a graphite electrode as a prototype, and a foamed nickel substrate as a cathode, and performing electrodeposition to prepare iron/foamed nickel electrode; (2) impregnation deposition, dissolving hexachloroplatinic acid in water to prepare an impregnation deposition solution, and then put the iron/nickel foam electrode into the impregnation deposition solution for reaction; (3) chemical reduction, weigh the hydroboration Sodium or potassium borohydride solution is dissolved in water to prepare a reducing agent solution, and then the reducing agent solution is added to the immersion deposition solution of the step (2) for reduction to obtain a platinum-iron/nickel electrode, that is, a Pt-Fe/Ni electrode. The invention adopts electrodeposition, dipping deposition and chemical reduction method to prepare Pt-modified electrode Pt-Fe/Ni, not only the preparation conditions are easy to control, but also Pt and Fe are loaded on foamed nickel in nanometer shape, which improves the surface area of the original platinum electrode material , to promote the electrocatalytic activity of the electrode.
Description
技术领域technical field
本发明涉及环境保护与治理领域,特别涉及一种铂改性材料的制备方法。The invention relates to the field of environmental protection and governance, in particular to a preparation method of a platinum modified material.
背景技术Background technique
四溴双酚A(tetrabromobisphenol A,TBBPA)是一种目前最常见的溴代阻燃剂,广泛应用于建筑材料、合成纤维纺织品、集成电路板和塑料制品中。近年来,TBBPA被认定是一种潜在的内分泌干扰物(endocrine disruptingchemicals,EDCs),其在环境中的难降解性、累积性及其生物毒性,亟需寻找快速高效降解的方法。Tetrabromobisphenol A (TBBPA) is currently the most common brominated flame retardant, widely used in building materials, synthetic fiber textiles, integrated circuit boards and plastic products. In recent years, TBBPA has been identified as a potential endocrine disrupting chemical (EDCs). Due to its refractory, accumulative and biological toxicity in the environment, it is urgent to find a rapid and efficient degradation method.
电化学方法是一种传统的水处理技术,凭借多功能性、高能源效率、环境兼容性以及容易控制等优点,具有广阔的应用前景。由于四溴双酚A中溴原子的电负性较大,使得氧化脱溴较为困难。因此,运用电化学中的电催化还原降解TBBPA成为一种新思路。电催化还原的机理主要为:在H2存在的条件下,催化金属吸附H2形成吸附态的[H],吸附态的[H]对R-X(X=F、Cl、Br)进行断裂,实现脱卤。Electrochemical method is a traditional water treatment technology with promising applications due to its versatility, high energy efficiency, environmental compatibility, and easy control. Oxidative debromination is difficult due to the high electronegativity of the bromine atom in tetrabromobisphenol A. Therefore, the use of electrocatalytic reduction in electrochemistry to degrade TBBPA has become a new idea. The mechanism of electrocatalytic reduction is mainly: in the presence of H2 , the catalytic metal adsorbs H2 to form [H] in the adsorbed state, and the [H] in the adsorbed state breaks RX (X=F, Cl, Br) to achieve Dehalogenation.
Pt不但能够促进析氢反应的进行,而且能够吸附活性氢原子有利于电催化还原降解TBBPA,但是由于铂是贵金属比较稀有,直接用铂作为电极所需的成本较高,不利于后续的扩大使用。Pt can not only promote the hydrogen evolution reaction, but also absorb active hydrogen atoms, which is beneficial to the electrocatalytic reduction and degradation of TBBPA. However, since platinum is a relatively rare noble metal, the cost of directly using platinum as an electrode is relatively high, which is not conducive to the subsequent expansion of use.
公开于该背景技术部分的信息仅仅旨在增加对本发明的总体背景的理解,而不应当被视为承认或以任何形式暗示该信息构成已为本领域一般技术人员所公知的现有技术。The information disclosed in this Background section is only for enhancing the understanding of the general background of the present invention and should not be taken as an acknowledgment or any form of suggestion that the information constitutes the prior art that is already known to those skilled in the art.
发明内容Contents of the invention
本发明的目的在于提供一种铂改性材料的制备方法,该方法制备的到的铂改性材料适用于四溴双酚A电催化还原的铂改性电极,降低Pt电极中Pt的使用量,提高体系的产氢和贮氢能力,为四溴双酚A的电催化还原提供足够的氢源,保证电催化还原降解四溴双酚A的快速、高效进行,同时由于体系自主产氢能力强,可以避免外加H2时的潜在危险。。The object of the present invention is to provide a kind of preparation method of platinum modified material, the platinum modified material prepared by this method is applicable to the platinum modified electrode of electrocatalytic reduction of tetrabromobisphenol A, reduces the usage amount of Pt in the Pt electrode , improve the hydrogen production and hydrogen storage capacity of the system, provide sufficient hydrogen source for the electrocatalytic reduction of tetrabromobisphenol A, ensure the rapid and efficient electrocatalytic reduction degradation of tetrabromobisphenol A, and at the same time, due to the independent hydrogen production capacity of the system Strong, can avoid the potential danger when adding H2. .
为实现上述目的,本发明提供了一种铂改性材料的制备方法,包括以下步骤:In order to achieve the above object, the invention provides a kind of preparation method of platinum modified material, comprising the following steps:
(1)电沉积,制备电沉积液,以石墨电极作为样机,泡沫镍基材作为阴极,进行电沉制备铁/泡沫镍电极;(1) Electrodeposition, preparation of electrodeposition solution, graphite electrode as prototype, foamed nickel substrate as cathode, electrodeposited to prepare iron/foamed nickel electrode;
(2)浸渍沉积,将六氯合铂氢酸(H2PtCl6)溶于水中,制备得到浸渍沉积液,然后将铁/泡沫镍电极置入浸渍沉积液中反应;(2) Immersion deposition, dissolving hexachloroplatinic acid (H 2 PtCl 6 ) in water to prepare an immersion deposition solution, and then putting the iron/foam nickel electrode into the immersion deposition solution to react;
(3)化学还原,称取硼氢化钠(NaBH4)或硼氢化钾(KBH4)溶液溶于水中制得还原剂溶液,然后将还原剂溶液加入所述步骤(2)的浸渍沉积液中还原,得到铂-铁/镍电极,即Pt-Fe/Ni电极。(3) Chemical reduction, taking sodium borohydride (NaBH 4 ) or potassium borohydride (KBH 4 ) solution and dissolving it in water to obtain a reducing agent solution, and then adding the reducing agent solution to the dipping deposition solution in step (2) Reduction, to obtain platinum-iron/nickel electrode, that is, Pt-Fe/Ni electrode.
优选地,上述方案中,所述电沉积液包括:七水硫酸亚铁(FeSO4·7H2O)、硫酸钠(Na2SO4)和十六烷基三甲基溴化铵(CTAB),七水硫酸亚铁、硫酸钠和十六烷基三甲基溴化铵的摩尔浓度比为5-25:1-15:1。Preferably, in the above scheme, the electrodeposition solution includes: ferrous sulfate heptahydrate (FeSO 4 ·7H 2 O), sodium sulfate (Na 2 SO 4 ) and cetyltrimethylammonium bromide (CTAB) , the molar concentration ratio of ferrous sulfate heptahydrate, sodium sulfate and cetyltrimethylammonium bromide is 5-25:1-15:1.
优选地,上述方案中,在进行电沉积前对泡沫镍基材进行预处理,包括以下步骤,首先对泡沫镍基材进行酸处理出去表面氧化层,然后在乙醇中进行超声处理,再置入水中进行超声处理。Preferably, in the above-mentioned scheme, the nickel foam substrate is pretreated before electrodeposition, including the following steps: first, the nickel foam substrate is acid-treated to remove the surface oxide layer, then ultrasonically treated in ethanol, and then placed in Sonication in water.
优选地,上述方案中,泡沫镍酸处理所用的酸为硫酸。Preferably, in the above scheme, the acid used for foam nickel acid treatment is sulfuric acid.
优选地,上述方案中,所述步骤(1)中电沉积的电流为10mA,电沉时间为20-40min。Preferably, in the above scheme, the electrodeposition current in the step (1) is 10mA, and the electrodeposition time is 20-40min.
优选地,上述方案中,所述步骤(2)中铁/泡沫镍电极置入浸渍沉积液中,然后置入振荡装置中反应。Preferably, in the above scheme, in the step (2), the iron/foam nickel electrode is placed in the immersion deposition solution, and then placed in an oscillating device for reaction.
优选地,上述方案中,所述的振荡装置为水浴振荡,振荡时温度为30-50℃、振荡速率为90-130r/min、振荡时间4-8h。Preferably, in the above solution, the oscillation device is a water bath oscillation, the oscillation temperature is 30-50°C, the oscillation speed is 90-130r/min, and the oscillation time is 4-8h.
优选地,上述方案中,所述步骤(2)中六氯合铂氢酸溶于水后制得六氯合铂氢酸溶液物质的量浓度为0.0001-0.001mol/L。Preferably, in the above scheme, the hexachloroplatinum hydrogen acid solution obtained after the hexachloroplatinum hydrogen acid is dissolved in water in the step (2) has a concentration of 0.0001-0.001mol/L.
优选地,上述方案中,所述步骤(3)中加入还原剂溶液的pH值为11-13。Preferably, in the above scheme, the pH value of the reducing agent solution added in the step (3) is 11-13.
优选地,上述方案中,所述步骤(3)中还原时间为30-60min。Preferably, in the above scheme, the reduction time in the step (3) is 30-60min.
与现有技术相比,本发明具有如下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
(1)本发明采用电沉积、浸渍沉积和化学还原法制备Pt改性电极Pt-Fe/Ni,不但制备条件易于控制,而且Pt、Fe呈纳米形状负载于泡沫镍上,提高了原铂电极材料的表面积,促进了电极的电催化活性。(1) The present invention prepares Pt-modified electrode Pt-Fe/Ni by electrodeposition, dipping deposition and chemical reduction, not only the preparation conditions are easy to control, but also Pt and Fe are loaded on foamed nickel in nanometer shape, which improves the efficiency of the original platinum electrode. The surface area of the material promotes the electrocatalytic activity of the electrode.
(2)过渡金属Fe加入Pt中一方面增强了Pt电极材料的电催化活性,另一方面减少了铂的使用量,降低了生成成本,有利于推广使用。(2) The addition of transition metal Fe to Pt enhances the electrocatalytic activity of the Pt electrode material on the one hand, and on the other hand reduces the amount of platinum used and the production cost, which is conducive to popularization and use.
(3)采用泡沫镍为贵金属Pt的基底材料,一方面由于泡沫镍具有刚性强、呈网状的结构特点增大了Pt改性电极的表面积,则有利于传质和提高了电极的电化学活性;另一方面采用Pt改性电极电催化还原降解四溴双酚A,可以解决Pt形成的二元催化剂难回收,造成二次污染的问题。(3) Nickel foam is used as the base material of noble metal Pt. On the one hand, the surface area of Pt modified electrode is increased due to the strong rigidity and network structure of nickel foam, which is beneficial to mass transfer and improves the electrochemical performance of the electrode. activity; on the other hand, the use of Pt modified electrode electrocatalytic reduction to degrade tetrabromobisphenol A can solve the problem that the binary catalyst formed by Pt is difficult to recycle and cause secondary pollution.
(4)NaBH4或KBH4对形成的Pt-Fe/泡沫Ni电极的再次还原,使得原来浸渍电极表面部分其他价态的铂离子得以形成纳米粒子负载于电极上,同时再次加固了铁的还原,减少了纳米铁的氧化,有利于对四溴双酚A的电催化还原降解,也提高了对铂盐的利用率。(4) Re-reduction of the formed Pt-Fe/Ni foam electrode by NaBH 4 or KBH 4 enables platinum ions in other valence states to be impregnated on the surface of the electrode to form nanoparticles loaded on the electrode, and at the same time strengthen the reduction of iron , reducing the oxidation of nano-iron, which is beneficial to the electrocatalytic reduction degradation of tetrabromobisphenol A, and also improves the utilization rate of platinum salt.
附图说明Description of drawings
图1是未经处理的泡沫镍电极的SEM图;Fig. 1 is the SEM figure of untreated foamed nickel electrode;
图2是经本发明的制备方法处理后制得Pt-Fe/Ni电极的SEM图;Fig. 2 is the SEM figure that makes Pt-Fe/Ni electrode after the preparation method of the present invention is processed;
图3是经本发明的制备方法处理后制得Pt-Fe/Ni电极的EDS图。Fig. 3 is an EDS diagram of a Pt-Fe/Ni electrode prepared after being processed by the preparation method of the present invention.
图4是经实施例1和实施例2的制备方法处理后制得Pt-Fe/Ni电极的电化学性能测试图。Fig. 4 is the electrochemical performance test diagram of the Pt-Fe/Ni electrode prepared after the preparation method of Example 1 and Example 2.
图5是经实施例3和实施例4的制备方法处理后制得铂改性电极的电化学性能测试图。Fig. 5 is an electrochemical performance test chart of a platinum-modified electrode prepared after being processed by the preparation methods of Example 3 and Example 4.
具体实施方式detailed description
下面结合附图,对本发明的具体实施方式进行详细描述,但应当理解本发明的保护范围并不受具体实施方式的限制。The specific embodiments of the present invention will be described in detail below in conjunction with the accompanying drawings, but it should be understood that the protection scope of the present invention is not limited by the specific embodiments.
除非另有其它明确表示,否则在整个说明书和权利要求书中,术语“包括”或其变换如“包含”或“包括有”等等将被理解为包括所陈述的元件或组成部分,而并未排除其它元件或其它组成部分。Unless expressly stated otherwise, throughout the specification and claims, the term "comprise" or variations thereof such as "includes" or "includes" and the like will be understood to include the stated elements or constituents, and not Other elements or other components are not excluded.
实施例1Example 1
Pt-Fe/Ni改性电极材料的制备过程,包括以下步骤:The preparation process of Pt-Fe/Ni modified electrode material comprises the following steps:
(1)基材预处理:首先,将泡沫镍基体材料剪成3cm×5cm大小,将剪裁好的泡沫镍基体材料置于1mol/L的H2SO4中处理5min,以除去表面的氧化层;随后,将经酸处理的泡沫镍基体依次在乙醇、去离子水中超声15min,除去表面的有机物;(1) Substrate pretreatment: First, cut the foamed nickel base material into a size of 3cm×5cm, and place the cut foamed nickel base material in 1mol/L H 2 SO 4 for 5 minutes to remove the oxide layer on the surface ; Subsequently, the acid-treated nickel foam matrix is ultrasonically 15min in ethanol and deionized water successively to remove organic matter on the surface;
(2)电沉积:配制100mL电沉积液,其溶液中FeSO4·7H2O、Na2SO4及CTAB的浓度分别为0.015mol/L、0.01mol/L及0.001mol/L,以惰性石墨电极为阳极,经预处理的泡沫镍基体材料为阴极,在室温条件下,以10mA的恒电流进行电沉30min制备Fe/泡沫镍电极;(2) Electrodeposition: prepare 100mL electrodeposition solution, the concentrations of FeSO 4 7H 2 O, Na 2 SO 4 and CTAB in the solution are 0.015mol/L, 0.01mol/L and 0.001mol/L respectively, with inert graphite The electrode is the anode, and the pretreated nickel foam base material is the cathode. At room temperature, the Fe/foam nickel electrode is prepared by electroplating at a constant current of 10mA for 30min;
(3)浸渍沉积:以水为溶剂,将H2PtCl6溶于其中,配制0.02mol/L的H2PtCl6贮备液,4℃保存;取储备液1.5mL稀释至50mL,配成浓度为0.0006mol/L的浸渍沉积液;将Fe/泡沫镍电极置于上述浸渍沉积液中,在温度30℃、转速130r/min恒定条件下,振荡4h;(3) Immersion deposition: use water as solvent, dissolve H 2 PtCl 6 in it, prepare 0.02mol/L H 2 PtCl 6 stock solution, store at 4°C; take 1.5mL of the stock solution and dilute it to 50mL, and make a concentration of 0.0006mol/L impregnation deposition solution; place the Fe/nickel foam electrode in the above impregnation deposition solution, and shake for 4 hours at a constant temperature of 30°C and a constant speed of 130r/min;
(4)化学还原:称取为铂和铁总物质的量6倍的NaBH4溶于10mL去离子水中,把其pH值调到12;将其还原剂溶液滴入浸渍沉积液中还原30min,得到Pt-Fe/Ni改性电极。(4) Chemical reduction: Dissolve NaBH 4 , which is 6 times the total amount of platinum and iron, in 10 mL of deionized water, and adjust its pH value to 12; drop its reducing agent solution into the dipping deposition solution for 30 min, A Pt-Fe/Ni modified electrode was obtained.
如图1为泡沫镍基底材料的扫描电镜图,泡沫镍表面光滑,是一种三维骨架结构,具有较大的孔容;图2为实施例1制得Pt-Fe/Ni改性电极的扫描电镜图,图中泡沫镍骨架上的纳米粒子更加密集,表明Pt、Fe纳米粒子均负载到其表面。Fig. 1 is the scanning electron micrograph of foamed nickel base material, foamed nickel surface is smooth, is a kind of three-dimensional skeleton structure, has larger pore volume; Fig. 2 is the scanning that embodiment 1 makes Pt-Fe/Ni modified electrode Electron micrographs, the nanoparticles on the nickel foam skeleton are denser, indicating that both Pt and Fe nanoparticles are loaded on the surface.
如图3所示为本实施例1制得Pt-Fe/Ni改性电极的EDS图,此图可以表明铂改性电极中存在O、Pt、Fe、Ni四种元素,则EDS图谱定性说明Pt、Fe已经成功负载到Pt-Fe/Ni电极表面。As shown in Figure 3, it is the EDS diagram of the Pt-Fe/Ni modified electrode prepared in Example 1. This diagram can show that there are four elements O, Pt, Fe, and Ni in the platinum modified electrode, and the EDS diagram is qualitatively illustrated Pt and Fe have been successfully loaded onto the surface of Pt-Fe/Ni electrodes.
在0.5mol/L H2SO4溶液条件下,以铂电极为对电极、饱和甘汞电极为参比电极及Pt-Fe/Ni改性电极为工作电极的三电极体系情况下,测定Pt-Fe/Ni改性电极的电催化性能。如图4所示为本实施例1制得的Pt-Fe/Ni电极的电化学性能测试图。Under the condition of 0.5mol/LH 2 SO 4 solution, in the case of a three-electrode system with a platinum electrode as the counter electrode, a saturated calomel electrode as the reference electrode and a Pt-Fe/Ni modified electrode as the working electrode, the determination of Pt-Fe Electrocatalytic performance of Ni/Ni modified electrodes. As shown in FIG. 4 , the electrochemical performance test chart of the Pt-Fe/Ni electrode prepared in Example 1 is shown.
实施例2Example 2
Pt-Fe/Ni改性电极材料的制备过程,包括以下步骤:The preparation process of Pt-Fe/Ni modified electrode material comprises the following steps:
(1)基材预处理:首先,将泡沫镍基体材料剪成3cm×5cm大小,将剪裁好的泡沫镍基体材料置于1mol/L的H2SO4中处理5min,以除去表面的氧化层;随后,将经酸处理的泡沫镍基体依次在乙醇、去离子水中超声15min,除去表面的有机物;(1) Substrate pretreatment: First, cut the foamed nickel base material into a size of 3cm×5cm, and place the cut foamed nickel base material in 1mol/L H 2 SO 4 for 5 minutes to remove the oxide layer on the surface ; Subsequently, the acid-treated nickel foam matrix is ultrasonically 15min in ethanol and deionized water successively to remove organic matter on the surface;
(2)电沉积:配制100mL电沉积液,其溶液中FeSO4·7H2O、Na2SO4及CTAB的浓度分别为0.015mol/L、0.01mol/L及0.001mol/L,以惰性石墨电极为阳极,经预处理的泡沫镍基体材料为阴极,在室温条件下,以10mA的恒电流进行电沉30min制备Fe/泡沫镍电极;(2) Electrodeposition: prepare 100mL electrodeposition solution, the concentrations of FeSO 4 7H 2 O, Na 2 SO 4 and CTAB in the solution are 0.015mol/L, 0.01mol/L and 0.001mol/L respectively, with inert graphite The electrode is the anode, and the pretreated nickel foam base material is the cathode. At room temperature, the Fe/foam nickel electrode is prepared by electroplating at a constant current of 10mA for 30min;
(3)浸渍沉积:以水为溶剂,将H2PtCl6溶于其中,配制0.02mol/L的H2PtCl6贮备液,4℃保存;取储备液0.75mL稀释至50mL,配成浓度为0.0003mol/L的浸渍沉积液;将Fe/泡沫镍电极置于上述浸渍沉积液中,在温度30℃、转速130r/min恒定条件下,振荡4h;(3) Immersion deposition: use water as solvent, dissolve H 2 PtCl 6 in it, prepare 0.02mol/L H 2 PtCl 6 stock solution, store at 4°C; take 0.75mL stock solution and dilute it to 50mL, and make a concentration of 0.0003mol/L impregnation deposition solution; place the Fe/nickel foam electrode in the above impregnation deposition solution, and shake for 4 hours at a constant temperature of 30°C and a constant speed of 130r/min;
(4)化学还原:称取为铂和铁总物质的量6倍的NaBH4溶于10mL去离子水中,把其pH值调到12;将其还原剂溶液滴入浸渍沉积液中还原30min,得到Pt-Fe/Ni改性电极。(4) Chemical reduction: Dissolve NaBH 4 , which is 6 times the total amount of platinum and iron, in 10 mL of deionized water, and adjust its pH value to 12; drop its reducing agent solution into the dipping deposition solution for 30 min, A Pt-Fe/Ni modified electrode was obtained.
在0.5mol/L H2SO4溶液条件下,以铂电极为对电极、饱和甘汞电极为参比电极及Pt-Fe/Ni改性电极为工作电极的三电极体系情况下,测定Pt-Fe/Ni改性电极的电催化性能。如图4所示为本实施例1制得的Pt-Fe/Ni电极的电化学性能测试图。Under the condition of 0.5mol/LH 2 SO 4 solution, in the case of a three-electrode system with a platinum electrode as the counter electrode, a saturated calomel electrode as the reference electrode and a Pt-Fe/Ni modified electrode as the working electrode, the determination of Pt-Fe Electrocatalytic performance of Ni/Ni modified electrodes. As shown in FIG. 4 , the electrochemical performance test chart of the Pt-Fe/Ni electrode prepared in Example 1 is shown.
实施例3Example 3
Pt-Fe/Ni改性电极材料的制备过程,包括以下步骤:The preparation process of Pt-Fe/Ni modified electrode material comprises the following steps:
(1)基材预处理:首先,将泡沫镍基体材料剪成3cm×5cm大小,将剪裁好的泡沫镍基体材料置于1mol/L的H2SO4中处理5min,以除去表面的氧化层;随后,将经酸处理的泡沫镍基体依次在乙醇、去离子水中超声15min,除去表面的有机物;(1) Substrate pretreatment: First, cut the foamed nickel base material into a size of 3cm×5cm, and place the cut foamed nickel base material in 1mol/L H 2 SO 4 for 5 minutes to remove the oxide layer on the surface ; Subsequently, the acid-treated nickel foam matrix is ultrasonically 15min in ethanol and deionized water successively to remove organic matter on the surface;
(2)电沉积:配制100mL电沉积液,其溶液中FeSO4·7H2O、Na2SO4及CTAB的浓度分别为0.015mol/L、0.01mol/L及0.001mol/L,以惰性石墨电极为阳极,经预处理的泡沫镍基体材料为阴极,在室温条件下,以10mA的恒电流进行电沉30min制备Fe/泡沫镍电极;(2) Electrodeposition: prepare 100mL electrodeposition solution, the concentrations of FeSO 4 7H 2 O, Na 2 SO 4 and CTAB in the solution are 0.015mol/L, 0.01mol/L and 0.001mol/L respectively, with inert graphite The electrode is the anode, and the pretreated nickel foam base material is the cathode. At room temperature, the Fe/foam nickel electrode is prepared by electroplating at a constant current of 10mA for 30min;
(3)浸渍沉积:以水为溶剂,将H2PtCl6溶于其中,配制0.02mol/L的H2PtCl6贮备液,4℃保存;取储备液1.5mL稀释至50mL,配成浓度为0.0006mol/L的浸渍沉积液;将Fe/泡沫镍电极置于上述浸渍沉积液中,在温度50℃、转速90r/min恒定条件下,振荡8h,得到Pt-Fe/Ni改性电极。(3) Immersion deposition: use water as solvent, dissolve H 2 PtCl 6 in it, prepare 0.02mol/L H 2 PtCl 6 stock solution, store at 4°C; take 1.5mL of the stock solution and dilute it to 50mL, and make a concentration of 0.0006mol/L impregnation deposition solution; place the Fe/nickel foam electrode in the above impregnation deposition solution, and vibrate for 8 hours at a constant temperature of 50°C and a speed of 90r/min to obtain a Pt-Fe/Ni modified electrode.
实施例4Example 4
Pt/Ni改性电极材料的制备过程,包括以下步骤:The preparation process of Pt/Ni modified electrode material comprises the following steps:
(1)基材预处理:首先,将泡沫镍基体材料剪成3cm×5cm大小,将剪裁好的泡沫镍基体材料置于1mol/L的H2SO4中处理5min,以除去表面的氧化层;随后,将经酸处理的泡沫镍基体依次在乙醇、去离子水中超声15min,除去表面的有机物;(1) Substrate pretreatment: First, cut the foamed nickel base material into a size of 3cm×5cm, and place the cut foamed nickel base material in 1mol/L H 2 SO 4 for 5 minutes to remove the oxide layer on the surface ; Subsequently, the acid-treated nickel foam matrix is ultrasonically 15min in ethanol and deionized water successively to remove organic matter on the surface;
(2)浸渍沉积:以水为溶剂,将H2PtCl6溶于其中,配制0.02mol/L的H2PtCl6贮备液,4℃保存;配制50mL的浸渍沉积液,其溶液中H2PtCl6浓度为0.0006mol/L,CTAB的浓度分别为0.001mol/L;将预处理的泡沫镍电极置于上述浸渍沉积液中,在温度30℃、转速130r/min恒定条件下,振荡4h;(2) Immersion deposition: use water as solvent, dissolve H 2 PtCl 6 in it, prepare 0.02mol/L H 2 PtCl 6 stock solution, store at 4°C ; 6 The concentration is 0.0006mol/L, and the concentration of CTAB is 0.001mol/L respectively; place the pretreated foamed nickel electrode in the above dipping deposition solution, and shake for 4 hours at a constant temperature of 30°C and a constant speed of 130r/min;
(3)化学还原:称取为铂物质的量6倍的NaBH4溶于10mL去离子水中,把其pH值调到12;将其还原剂溶液滴入浸渍沉积液中还原30min,得到Pt/Ni改性电极。(3) Chemical reduction: Dissolve NaBH 4 , which is 6 times the amount of platinum substance, in 10 mL of deionized water, and adjust its pH value to 12; drop its reducing agent solution into the dipping deposition solution for 30 min to obtain Pt/ Ni modified electrode.
在四溴双酚A初始浓度20mg/L,初始pH=3的条件下,以铂电极为对电极、饱和甘汞电极为参比电极及Pt-Fe/泡沫镍电极或Pt/泡沫镍电极为工作电极的三电极体系情况下,测定铂改性电极的对四溴双酚A的电催化性能。本方法对实施例3和实施例4的制得的铂改性电极进行测试。如图5Pt/Ni电极及Pt-Fe/Ni电极在TBBPA存在条件下的电化学阻抗谱。Pt-Fe/Ni电极的电阻抗小于Pt/Ni电极的电阻抗,电阻抗越小,电子在电极表面的迁移速率越快。由电化学阻抗谱可以得出,Fe纳米粒子的加入可以减少电极的阻抗,加速电子在电极表面的迁移速率。Under the conditions of initial tetrabromobisphenol A concentration of 20mg/L and initial pH=3, a platinum electrode is used as a counter electrode, a saturated calomel electrode is used as a reference electrode and a Pt-Fe/nickel foam electrode or a Pt/nickel foam electrode is In the case of the three-electrode system of the working electrode, the electrocatalytic performance of the platinum-modified electrode for tetrabromobisphenol A was determined. In this method, the platinum modified electrodes prepared in Example 3 and Example 4 were tested. As shown in Figure 5, the electrochemical impedance spectroscopy of Pt/Ni electrode and Pt-Fe/Ni electrode in the presence of TBBPA. The electrical impedance of the Pt-Fe/Ni electrode is smaller than that of the Pt/Ni electrode, and the smaller the electrical impedance, the faster the electron transfer rate on the electrode surface. It can be concluded from the electrochemical impedance spectroscopy that the addition of Fe nanoparticles can reduce the impedance of the electrode and accelerate the migration rate of electrons on the electrode surface.
前述对本发明的具体示例性实施方案的描述是为了说明和例证的目的。这些描述并非想将本发明限定为所公开的精确形式,并且很显然,根据上述教导,可以进行很多改变和变化。对示例性实施例进行选择和描述的目的在于解释本发明的特定原理及其实际应用,从而使得本领域的技术人员能够实现并利用本发明的各种不同的示例性实施方案以及各种不同的选择和改变。本发明的范围意在由权利要求书及其等同形式所限定。The foregoing descriptions of specific exemplary embodiments of the present invention have been presented for purposes of illustration and description. These descriptions are not intended to limit the invention to the precise form disclosed, and obviously many modifications and variations are possible in light of the above teaching. The exemplary embodiments were chosen and described in order to explain the specific principles of the invention and its practical application, thereby enabling others skilled in the art to make and use various exemplary embodiments of the invention, as well as various Choose and change. It is intended that the scope of the invention be defined by the claims and their equivalents.
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Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101157043A (en) * | 2007-09-26 | 2008-04-09 | 山东大学 | A kind of core-shell nanoporous metal catalyst and preparation method thereof |
| CN101455970A (en) * | 2008-11-19 | 2009-06-17 | 南京航空航天大学 | Preparation method of carbon supported core-shell Ni-Pt particles for direct methanol fuel cells |
| CN101642714A (en) * | 2009-09-02 | 2010-02-10 | 山东大学 | Preparation method of core-shell Fe/Pd bimetallic nano-catalyst |
| CN102009186A (en) * | 2010-12-30 | 2011-04-13 | 南京大学 | Low-cost tree-like Co-Pt core shell structure bimetallic material and preparation method thereof |
| CN103111307A (en) * | 2013-02-27 | 2013-05-22 | 江苏大学 | Preparation method of graphene supported nickel/platinum core-shell nano compound |
| CN103272615A (en) * | 2013-05-27 | 2013-09-04 | 浙江大学 | Preparation method of catalysts for oxygen production implemented through decomposition of hydrogen peroxide |
| CN103877993A (en) * | 2014-01-25 | 2014-06-25 | 陕西师范大学 | Ultrathin metal layer catalyst and application thereof |
| CN104857973A (en) * | 2015-04-28 | 2015-08-26 | 华南理工大学 | Supported catalyst with kernel-shell structure, preparation method thereof and application |
| CN104907081A (en) * | 2015-04-29 | 2015-09-16 | 陕西师范大学 | Efficient ultra-thin metal layer catalyst and use thereof |
| CN104947142A (en) * | 2015-05-29 | 2015-09-30 | 广西大学 | Preparation method of electrocatalytic reduction halogenated organic matter cathode material |
| CN104961199A (en) * | 2015-06-23 | 2015-10-07 | 广西大学 | Preparation method of Pd-Fe/foamed nickel three-dimensional particle electrodes |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9005331B2 (en) * | 2004-12-22 | 2015-04-14 | Brookhaven Science Associates, Llc | Platinum-coated non-noble metal-noble metal core-shell electrocatalysts |
| WO2012011170A1 (en) * | 2010-07-21 | 2012-01-26 | トヨタ自動車株式会社 | Fine catalyst particles and method for producing fine catalyst particles |
| US9472811B2 (en) * | 2011-02-15 | 2016-10-18 | GM Global Technology Operations LLC | Graphite particle-supported Pt-shell/Ni-core nanoparticle electrocatalyst for oxygen reduction reaction |
-
2016
- 2016-04-25 CN CN201610259868.2A patent/CN105839150B/en active Active
Patent Citations (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101157043A (en) * | 2007-09-26 | 2008-04-09 | 山东大学 | A kind of core-shell nanoporous metal catalyst and preparation method thereof |
| CN101455970A (en) * | 2008-11-19 | 2009-06-17 | 南京航空航天大学 | Preparation method of carbon supported core-shell Ni-Pt particles for direct methanol fuel cells |
| CN101642714A (en) * | 2009-09-02 | 2010-02-10 | 山东大学 | Preparation method of core-shell Fe/Pd bimetallic nano-catalyst |
| CN102009186A (en) * | 2010-12-30 | 2011-04-13 | 南京大学 | Low-cost tree-like Co-Pt core shell structure bimetallic material and preparation method thereof |
| CN103111307A (en) * | 2013-02-27 | 2013-05-22 | 江苏大学 | Preparation method of graphene supported nickel/platinum core-shell nano compound |
| CN103272615A (en) * | 2013-05-27 | 2013-09-04 | 浙江大学 | Preparation method of catalysts for oxygen production implemented through decomposition of hydrogen peroxide |
| CN103877993A (en) * | 2014-01-25 | 2014-06-25 | 陕西师范大学 | Ultrathin metal layer catalyst and application thereof |
| CN104857973A (en) * | 2015-04-28 | 2015-08-26 | 华南理工大学 | Supported catalyst with kernel-shell structure, preparation method thereof and application |
| CN104907081A (en) * | 2015-04-29 | 2015-09-16 | 陕西师范大学 | Efficient ultra-thin metal layer catalyst and use thereof |
| CN104947142A (en) * | 2015-05-29 | 2015-09-30 | 广西大学 | Preparation method of electrocatalytic reduction halogenated organic matter cathode material |
| CN104961199A (en) * | 2015-06-23 | 2015-10-07 | 广西大学 | Preparation method of Pd-Fe/foamed nickel three-dimensional particle electrodes |
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