WO2005092784A1 - Synthese de nanoparticules de platine et de palladium de la taille d'un puits quantique - Google Patents

Synthese de nanoparticules de platine et de palladium de la taille d'un puits quantique Download PDF

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WO2005092784A1
WO2005092784A1 PCT/IN2004/000072 IN2004000072W WO2005092784A1 WO 2005092784 A1 WO2005092784 A1 WO 2005092784A1 IN 2004000072 W IN2004000072 W IN 2004000072W WO 2005092784 A1 WO2005092784 A1 WO 2005092784A1
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platinum
palladium
nano particles
ethylene glycol
range
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PCT/IN2004/000072
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English (en)
Inventor
Madan Lal Singla
Mewa Singh
Dharam Veer Singh Jain
Ram Kishore
Ram Prakash Bajpai
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Council Of Scientific & Industrial Research
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Priority to PCT/IN2004/000072 priority Critical patent/WO2005092784A1/fr
Priority to CNA2004800428894A priority patent/CN1946628A/zh
Publication of WO2005092784A1 publication Critical patent/WO2005092784A1/fr

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    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/02Elements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/38Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
    • B01J23/40Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals of the platinum group metals
    • B01J23/44Palladium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/20Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state
    • B01J35/23Catalysts, in general, characterised by their form or physical properties characterised by their non-solid state in a colloidal state
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/30Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
    • B01J35/391Physical properties of the active metal ingredient
    • B01J35/393Metal or metal oxide crystallite size
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/16Reducing
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B82NANOTECHNOLOGY
    • B82YSPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
    • B82Y30/00Nanotechnology for materials or surface science, e.g. nanocomposites
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B29/00Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape
    • C30B29/60Single crystals or homogeneous polycrystalline material with defined structure characterised by the material or by their shape characterised by shape
    • C30B29/605Products containing multiple oriented crystallites, e.g. columnar crystallites
    • CCHEMISTRY; METALLURGY
    • C30CRYSTAL GROWTH
    • C30BSINGLE-CRYSTAL GROWTH; UNIDIRECTIONAL SOLIDIFICATION OF EUTECTIC MATERIAL OR UNIDIRECTIONAL DEMIXING OF EUTECTOID MATERIAL; REFINING BY ZONE-MELTING OF MATERIAL; PRODUCTION OF A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; SINGLE CRYSTALS OR HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; AFTER-TREATMENT OF SINGLE CRYSTALS OR A HOMOGENEOUS POLYCRYSTALLINE MATERIAL WITH DEFINED STRUCTURE; APPARATUS THEREFOR
    • C30B7/00Single-crystal growth from solutions using solvents which are liquid at normal temperature, e.g. aqueous solutions
    • C30B7/02Single-crystal growth from solutions using solvents which are liquid at normal temperature, e.g. aqueous solutions by evaporation of the solvent
    • C30B7/06Single-crystal growth from solutions using solvents which are liquid at normal temperature, e.g. aqueous solutions by evaporation of the solvent using non-aqueous solvents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/12Silica and alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/02Impregnation, coating or precipitation
    • B01J37/0215Coating

Definitions

  • TECHNICAL FIELD The present relates to a novel process for synthesis of platinum and palladium quantum well size nano-particles in ethylene gylcol medium in which ethylene glycol acts as a combined dispersing medium, reducing agent and capping agent.
  • BACKGROUND OF THE INVENTION The synthesis and properties of nano particles have commercial importance due to their potential utilization in catalysis, optoelectronic devices, photonics, magnetic and ultra sensitive chemical sensors. Many gas phase catalytic processes exhibit a pronounced, particle size dependence of catalytic activity.
  • the nano particles possess a very large surface to volume ratio; consequently the surface chemistry of nano-particles plays an important role. Control of particle size, the size distribution and particle shape leads to understanding of their specific properties.
  • the nano particles may consist of metals, ceramics and semi-conductors or even composites.
  • a number of methods such as photolytic reduction, radiolytic reduction, sono-chemical reduction method, micro emulsion technique, polyol process, reduction by alcohol and many other methods have been used for the synthesis of Pt & Pd metal nanoparticles.
  • different capping agents have been used alongwith different reducing agents. These capping agents are highly costly and perform under restricted conditions. Moreover, sometimes these add certain impurities also.
  • the Inventors adopt a simple process for the synthesis of Pt, Pd, and Au nano particles using ethylene glycol or glycerol where the same substance acts as dispersing media, self reducing agent and also capping agent.
  • alkane-thiols with various chain lengths (C 3 - C 24 ) and perfluorinated thiols to produce and cap metal nano particles. These involve reduction of metal salts at controlled pH and stabilization in aqueous or organic layer capping with thiol. Number of alkane-thiol have been used as capping agent to provide protecting properties for metal core (Pt, Pd, Au) and allow reasonable solubility in non polar organic solvents.
  • the reported polymers are poly vinylpyriOlidone, poly dithiofulvene, Dendrimers N-isopropylacylamide, chitosan, N-isopropylacrylamide polymer [PNIPA Am-Pfj. N-vinylisobutyramide has been used for encapsulating nanoparticles. These systems produce nano particles with large variation in nano sizes. Colloidal Platinum nano particles in the range of 10-30A were reported in ethanol water mixture in the presence of Poly (N-vinylisobutyramide) (PNVIBA).
  • Thiol functionalised platinum nano particles have been prepared in tetra-hydrofuoran as dispersing medium, lithium-triethyl borohydride as reducing agent and octadecanthiol as stabilizing agent.
  • the size of nano particles is around 3 nm.
  • this method involves the use of a large number of reagents besides this method is quite tedious.
  • Chitosan is a natural polymer which has been used for synthesis Pt, Pd nano particles using hydrazine or borohydride as reducing agent .
  • the diameter of the nano particles is around 3nm, however, synthesis involves the use number of number of reagents.
  • Regular Pt nano particles have been obtained by epitaxial deposition on NaCl surfaces supported by thin film of Ceria subject to hydrogen reduction up to 1073K.
  • a reference may be made to Take Fujimoto, etal ;Scripta Materialial 44,( 2001), P 2183-860.
  • the size of nano particles according to the above reference was found to be 10-15 nm. This process needs high cost equipment and vacuum of the order of 10 ⁇ 6 m bar.
  • Au nano particles have been prepared by sono- chemical reduction in aqueous medium where metal salt, surfactant, reducing agent are being used.
  • a multi wave ultra sound generator with a barium titanate oscillator has been used for sonif ⁇ cation.
  • the particle size is formed 2 to 10 nm.
  • a reference may be made to Chen. D.H. J. Collid interface Science Vol. 219, P 123-129, 155-166, 1999 in this regard.
  • Pt- Ni nano particles were prepared by hydrazine reduction of the metal salts by prolonged reaction at room temperature and microwave assisted reduction.
  • a reference may be made to O.P. Yadav etal, Colloids & Surfaces 221(2003), P 131-134. According to this reference, the average particle size is 2.9 to 5.8 nm.
  • the Pt, Pd nano particles have also been prepared by the reduction of metal ions with hydrazine or Borohydride in oil water micro emulsion and consisting of AOT or other surfactants, cyclohexane and aqueous solution of metal salt varying compositions. These nano particles are stable in micro-emulsion On breaking, the micro-emulsion nano particles start coagulating resulting in increase in size. The technique involves high cost of synthesis as well as a large number of reagents.
  • the main object of the present invention is synthesis of Pt and Pd metal nano particles of quantum well size around 3 nm in ethylene glycol medium, in which ethylene glcycol acts both as reducing and capping agent.
  • Another object of the present invention is that the nano particles do not aggloramate for long storage.
  • Another objective of the present invention is that nano particles do not get oxidized on centrifugation or during synthesis.
  • Another objective of the present invention is that nano particle should be free of impurities.
  • nano particles should work as better catalyst due to large surface area.
  • nano particles may get adsorbed on surface like silica, alumina or porous materials for their use in opto-electonic devices/catalysis.
  • nano particles of varying size can be prepared by varying the composition of the reaction mixture.
  • Yet another objective of the present invention is to synthesize the nano particles at much faster rate than the existing methods.
  • the present invention relates to a process for the synthesis of platinum and palladium quantum well size nano-particles in ethylene gylcol medium in which ethylene glycol acts as a combined dispersing medium, reducing agent and capping agent.
  • the present invention provides a process for preparing quantum well size nano particles of platinum / palladium having particle size in the range of 2 to 10 nm, said process comprising the steps of adding ethylene glycol / glycerol to platinum / palladium , salt solution, wherein ethylene glycol / glycerol acts as a combined dispersing medium, reducing agent and capping agent.
  • ethylene glycol / glycerol acts as a combined dispersing medium, reducing agent and capping agent.
  • a mixture of ethylene glycol / glycerol and platinum / palladium salt solution is heated to a temperature in the range of 105° to 140°C to obtain nano particles of platinum / palladium and a mother liquor.
  • the platinum salt solution used is an aqueous solution of H 2 PtCl 6 .6H 2 O.
  • the palladium salt solution used is an aqueous solution of PdCl 2 .
  • the concentration of platinum / palladium to ethylene glycol / glycerol is in the range of 0.025 to 1%.
  • the mixture of ethylene glycol / glycerol and platinum / palladium salt solution is mixed by stirring for a time period of about 30 about minutes and the pH of the solution is maintained between 4 to 6.
  • the mixture of ethylene glycol / glycerol and platinum / palladium salt solution is a clear transparent solution having an absorption peask for Pt(IV) in ethylene glycol medium at 265nm and at 221 nm for Pd(II).
  • the mixture of ethylene glycol / glycerol and platinum salt solution is heated to a temperature in the range of 130° to 140°C till the mixture initially turns brown and then black.
  • the mixture of ethylene glycol / glycerol and platinum salt solution is heated to a temperature in the range of 130° to 140°C for a time period in the range of 5 to 7 minutes.
  • the mixture of ethylene glycol / glycerol and palladium salt solution is heated to a temperature in the range of 105° to 110°C till the mixture initially turns brown and then black.
  • the mixture of ethylene glycol / glycerol and palladium salt solution is heated to a temperature in, the range of 105° to 110°C for a time period in the range of 5 to 7 minutes.
  • the nano particles of platinum is heated to a temperature in the range of 130° to 140°C for a time period in the range of 5 to 7 minutes.
  • the size of palladium nano particles thus obtained is in the range of 2 to 6nm for solution concentration in the range of 5 to 25 mg of palladium nano particles.
  • the present invention more particularly provides a process for preparing quantum well size nano particles of platinum / palladium having particle size in the range of 2 to 10 nm, said process comprising the steps of adding ethylene glycol / glycerol to platinum / palladium salt solution, wherein ethylene glycol / glycerol acts as a combined dispersing medium, reducing agent and capping agent and heating the same at a temperature in the range of
  • reaction mixture has been stirred for 30 minutes.
  • nano particles are formed at temperature 130°C -140°C for Pt and l05°C - 110°C for Pd by keeping it for 3-7 minutes.
  • the nano particles have been characterized by UV- Visible Spectroscopy, Transmission Electron Microscopy, Electron diffraction analysis, XRD & FTIR.
  • these nano particles have been separated from reacting mixture by centrifugation at a speed of 10,000 revolution per minute.
  • Pt & Pd nano particles have been dispersed in different solvent like ethylene glycol, glycerine & alcohols.
  • Pt & Pd nano particles have been coated on alumina and silica mesh size 230-400.
  • these nano particles has been used for catalytic use.
  • other polyhydric alcohols like glycerol and erythritrol has been used for synthesis of these nano particles.
  • Figure 1(a) represents the TEM micrograph of platinum solution containing 5 mg of platinum. As can be seen, the magnification is 3,90,000 times and the particle size was determined to be equal to about 4 nm.
  • Figure 1(b) represents the Electron diffraction pattern of nanoparticles obtained using platinum solution containing 5 mg of platinum.
  • Figure 2(a) represents the TEM micrograph of platinum solution containing 10 mg of platinum. As can be seen, the magnification is 5,20,000 times and the particle size was determined to be equal to about 3 nm.
  • Figure 2(b) represents the Electron diffraction pattern of nanoparticles obtained using platinum solution containing 10 mg of platinum.
  • Figure 3(a) represents the TEM micrograph of platinum solution containing 15 mg of platinum. As can be seen, the magnification is 5,20,000 times and the particle size was determined to be equal to about 3 nm.
  • Figure 3(b) represents the Electron diffraction pattern of nanoparticles obtained using platinum solution containing 15 mg of platinum.
  • Figure 4(a) represents the TEM micrograph of palladium solution containing 10 mg of palladium. As can be seen, the magnification is 3,90,000 times and the particle size was determined to be in the range of 2 to 6 nm.
  • Figure 4(b) represents the Electron diffraction pattern of nanoparticles obtained using palladium solution containing 10 mg of platinum.
  • reaction mixture was stirred for 30 minutes at room temperature. There is no immediate colour change at room temperature.
  • the reaction mixture was heated to 130°C - 140 °C for Pt and 105°C- 110°C for Pd for 3-7 minutes. On heating the colour of mixture first turn brown and finally black. The complete reduction was confirmed from the absorption spectra. It may be noted that no inert atmosphere has been used during the reaction.
  • the Inventors have also find that the method is quite general for production of nano particles of metals from their ions in higher oxidation state provided the sum of the Gibbs enegy for reduction of metal ions and Gibbs energy for the oxidation of glycol to glyoxal is negative.
  • the Inventors also note that a number of polyhydric alcohols like glycerol and eiythritrol are also suitable for production and capping of metal nano particles. Change in the absorption Spectral with Reduction UV & Visible spectral changes were recorded during the reduction of Pt & Pd ions in ethylene glycol.
  • the spectral of the solution consists of a major peak at 265 nm attributed to Pt Cl 6 "2 ion or 221 nm PdCl 2 .
  • the peak at 265 nm & 221 nm disappear indicating the complete formation of Pt (0) & Pd (0)
  • the colour of the solution also turns black.
  • the Pt - ethyleneglycol or Pd- ethylene glycol nano particles are highly stable and can be dispersed in ethylene glycol, glycerine and alcohols after the removal of excess ethyleneglycol.
  • Typical electron micrographs of ethylene glycol Pt, ethylene glycol Pd colloids are shown in figure.
  • the particle size and size distribution of colloidal Pt & Pd nanoparticles derived from TEM measurement are also shown in f ⁇ gure(Figla-4a).
  • TEM image reveals that well dispersed ethylene glycol — Pt nano particles lie between 3 to 4 nm for 5 to 15 mg of Pt concentration (fig la-3a). The Pd nano particles are found to be higher around 2-6 nm.
  • Platinum system - detail study of diffraction pattern of the corresponding area reveals the formation of single phase cubic platinum nano particles (hid) planes with strong deflection (100) and moderate (200).
  • Pd (220) is a strong crystalline cubic plan with weak
  • Alumina or silica in the ratio 100:1 Al 2 O :Pt or Pd is added in Pt(0), Pd (0) colloidal solution.
  • the dispersion mixture is stirred for half an hour and kept for 24 hours so that metal particles get adsorbed on the surface on the alumina or silica surface.
  • Pt or Pd adsorbed nano particles are separated after centrifugation and calcined at 500°C for one hour. After cooling these materials are stored in vacuum desiccators. XRD pattern showed the coated Pt or Pd nano particles on alumina and silica.
  • Example No. 1 Experiments were carried out to prepare Platinum and palladium nano particles using concentration of 5,10andl5 mg of Pt and 10,15 and20 mg of Pd in ethylene glycol medium. It has been observed that nano particles are formed of uniform size under controlled conditions of temperature. The size of pt nanoparticles lies between 3 to4 nm where as in case of pd it lies between 2 to 6nm.
  • Example No. 2 UV & Visible Spectroscopy was carried out and that there is no absorption peak at 265 nm for Pt (0) and 221 nm Pd (0), which was observed in ethylene glycol for metal chloride before the reduction process, starts.
  • Example No. 3 Transmission and electron diffraction studies were earned out which confirm the formation of nano particles of Quantum size. Electron diffraction studies indicate that the nano particles are monodispersive, single-phase cubic.
  • Example No. 4 The Inventors have separated the Pt & Pd nano particle from ethylene glycol by centifiguration and dispersed the same in different solvents. The Inventors have coated these nano particles on silica & alumina.
  • Example No. 5 The Inventors have tried to use these nano particles as catalyst for conversion of CO into carbon dioxide and other organic reactions and found that their results are far better than those obtained in conventional processes.

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  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Crystallography & Structural Chemistry (AREA)
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  • Nanotechnology (AREA)
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Abstract

L'invention concerne un procédé permettant de préparer des nanoparticules de platine/palladium de la taille d'un puits quantique comprise entre 2 et 10 nm. Ledit procédé consiste à ajouter un éthylène glycol/glycérol à une solution de sels de platine/palladium, l'éthylène glycol/glycérol agissant comme un milieu de dispersion combiné, un agent de réduction et un agent de coiffage; et à les chauffer à une température comprise entre 100° et 140 °C afin d'obtenir des nanoparticules de platine/palladium.
PCT/IN2004/000072 2004-03-29 2004-03-29 Synthese de nanoparticules de platine et de palladium de la taille d'un puits quantique WO2005092784A1 (fr)

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PCT/IN2004/000072 WO2005092784A1 (fr) 2004-03-29 2004-03-29 Synthese de nanoparticules de platine et de palladium de la taille d'un puits quantique
CNA2004800428894A CN1946628A (zh) 2004-03-29 2004-03-29 量子阱大小的铂和钯纳米颗粒的合成

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Cited By (3)

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US7829496B2 (en) * 2005-12-28 2010-11-09 Industrial Technology Research Institute Process for preparing platinum based electrode catalyst for use in direct methanol fuel cell
KR20160071198A (ko) 2014-12-11 2016-06-21 서강대학교산학협력단 팔라듐 나노 입자의 제조방법
CN113953526A (zh) * 2021-10-25 2022-01-21 昆明理工大学 一种超细钯粉的制备方法

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CN102205421A (zh) * 2010-03-31 2011-10-05 中国科学院福建物质结构研究所 水热法制备金、银纳米颗粒
CN108855240B (zh) * 2018-06-25 2020-11-20 厦门大学 一种利用甘油保护纳米铂颗粒催化活性的方法
CN115446303B (zh) * 2022-09-16 2024-01-16 中国人民解放军国防科技大学 一种铂量子点及其简易制备方法和应用

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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US7829496B2 (en) * 2005-12-28 2010-11-09 Industrial Technology Research Institute Process for preparing platinum based electrode catalyst for use in direct methanol fuel cell
US8012905B2 (en) 2005-12-28 2011-09-06 Industrial Technology Research Institute Process for preparing platinum based electrode catalyst for use in direct methanol fuel cell
KR20160071198A (ko) 2014-12-11 2016-06-21 서강대학교산학협력단 팔라듐 나노 입자의 제조방법
CN113953526A (zh) * 2021-10-25 2022-01-21 昆明理工大学 一种超细钯粉的制备方法
CN113953526B (zh) * 2021-10-25 2024-03-15 昆明理工大学 一种超细钯粉的制备方法

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