CN100588459C - Reverse micelle method for preparing platinum ruthenium/carbon catalyst - Google Patents

Reverse micelle method for preparing platinum ruthenium/carbon catalyst Download PDF

Info

Publication number
CN100588459C
CN100588459C CN200710060188A CN200710060188A CN100588459C CN 100588459 C CN100588459 C CN 100588459C CN 200710060188 A CN200710060188 A CN 200710060188A CN 200710060188 A CN200710060188 A CN 200710060188A CN 100588459 C CN100588459 C CN 100588459C
Authority
CN
China
Prior art keywords
minutes
aqueous solution
water
reverse micelle
carbon black
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN200710060188A
Other languages
Chinese (zh)
Other versions
CN101214437A (en
Inventor
田建华
赵沧燕
徐云飞
单忠强
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tianjin University
Original Assignee
Tianjin University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tianjin University filed Critical Tianjin University
Priority to CN200710060188A priority Critical patent/CN100588459C/en
Publication of CN101214437A publication Critical patent/CN101214437A/en
Application granted granted Critical
Publication of CN100588459C publication Critical patent/CN100588459C/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/50Fuel cells

Landscapes

  • Catalysts (AREA)

Abstract

The invention discloses a reverse micelles method of preparing platinum ruthenium/carbon catalyst, which includes the following steps: 0.02 to 0.10mol/L chloroplatinic acid aqueous solution and 0.04 to 0.20 mol/L ruthenium trichloride aqueous solution are prepared to form water phase; hexamethylene is prepared into oil phase, sodium laurylsulfate is taken as surfactant and n-octyl alcohol is takenas cosurfactant; the mass ratio of sodium laurylsulfate, hexamethylene and n-octyl alcohol is 1:0.07 to 0.15:0.5 to 1.2; the product is mixed and added in carbon black, and the receives ultrasonic vibration and mechanical mixing for 20 to 60 min, so that a reverse micelle is loaded on the carbon black; a reducing agent, demulsifier acetone and solution are added for filtration and drying. The reverse micelle of the invention provides a micro environment, and can become an ideal place of nano particle synthetization. Because of the method of preparing nano particles, only simple equipments areneeded, the operation is under room temperature, the metal particles have grain size which is easy to be controlled and spread quite evenly.

Description

The inverse micelle method of preparation platinum ruthenium/carbon catalyst
Technical field
The present invention relates to the Proton Exchange Membrane Fuel Cells technical field, also can be widely used in other chemical field.The present invention be more particularly directed to a kind of preparation carbon and carry the reverse micelle method of platinum ruthenium (PtRu/C) catalyst.
Background technology
Fuel cell is a kind of efficient, eco-friendly TRT, and the chemical energy that it directly will be stored in fuel and the oxidant is converted into electric energy.In today that environment and the energy receive much concern, the research and development of fuel cell more and more are subjected to the attention of national governments.
Proton Exchange Membrane Fuel Cells (PEMFC) has the energy conversion efficiency height, and specific energy is big, start rapidly and series of advantages such as environmental friendliness, and be following most effective and one of the generation technology that cleans most.Membrane electrode (Membrane﹠amp; Electrode Assembly is the parts of PEMFC most critical MEA), is the core that the PEMFC electrochemical reaction can efficiently be carried out, and membrane electrode is made up of diffusion layer, catalyst layer and PEM usually.Eelctro-catalyst adopts load type platinum/carbon (Pt/C) or platinum-ruthenium/carbon (Pt-Ru/C), and wherein the Pt-Ru/C catalyst also is the first-selected eelctro-catalyst of DMFC (DMFC).The general perfluorinated sulfonic acid type PEM (as the Nafion series membranes of du pont company) that adopts of PEM with high proton conductivity.
Eelctro-catalyst is to make among the PEMFC fuel and oxidant finish oxidation and reduction reaction conditio sune qua non respectively.Precious metals pt is the highest and stable catalyst to the reduction reaction activity of the oxidation reaction of hydrogen and oxygen up to now, so the first-selected Pt of PEMFC catalyst is catalyst based.But, adopt the PEMFC of the hydrogen of natural gas or liquid fuel reformation generation to exist Pt to cause the problem of power decline because of CO poisons.The eelctro-catalyst that exploitation has good resistance CO poisoning performance is to address this problem important method.The PtRu eelctro-catalyst is considered to one of best anti-CO poisoned catalyst at present.Studies show that in the Pt-Ru/C catalyst, the electronic section on the Ru atom is transferred on the Pt atom, thereby make it show the concerted catalysis effect.And Ru can make water decomposition form the oxygenated species (OH) of ADSORPTION STATE Ads, (OH) AdsCan oxidation be adsorbed on the CO toxin on the catalytic active site, make catalyst possess certain tolerance limit ability CO
Prepare highly active PtRu/C catalyst and be always the hot subject of PEMFC in recent years.At present the more Pt-Ru/C Preparation of catalysts method of report has inorganic colloid method, infusion process, gel sol method and the precipitation method etc., and there is the particle bad dispersibility in the catalyst of these original methods preparations, and the inhomogeneous and reaction condition of particle diameter is problem such as harshness relatively.Because Preparation of catalysts technology determines its The Nomenclature Composition and Structure of Complexes, and then influences its performance (comprising activity, life-span and utilization rate etc.), research PtRu/C Preparation of catalysts method and technology are extremely important.
Summary of the invention
The present invention proposes a kind of inverse micelle method for preparing platinum ruthenium/carbon catalyst, and step is as follows:
1) the configuration concentration scope is 0.02~0.10mol/L chloroplatinic acid aqueous solution, and the configuration concentration scope is 0.04~0.20mol/L ruthenium trichloride aqueous solution, and two kinds of solution constitute water jointly;
2) cyclohexane is an oil phase, and lauryl sodium sulfate is a surfactant, and n-octyl alcohol is a cosurfactant; The mass ratio of lauryl sodium sulfate and cyclohexane and n-octyl alcohol is 0.07~0.15: 0.5~1.2;
3) above-mentioned steps 2) sonic oscillation or mechanical agitation 15~40 minutes, drip the step 1) water then continuously, the mol ratio of water and surfactant should be 4~11; Ultrasonic concussion 20~60 minutes forms transparent reverse micelle system;
4) in above-mentioned steps 3) add carbon black in the described system, ultrasonic concussion or mechanical agitation 20~60 minutes load on the carbon black reverse micelle;
5) in above-mentioned steps 4) add reducing agent in the described system, reacted 20~40 minutes under mechanical agitation or the ultrasonic oscillation condition, continued stirring reaction 1~2 hour; Reducing agent adopts potassium borohydride or sodium borohydride aqueous solution, and consumption is 3~15 times of theoretical value, and volume is 3) 0.5 ~ 2 times of described water volume;
6) stir or the ultrasonic oscillation condition under add demulsifier acetone or absolute ethyl alcohol, addition is to leave standstill behind 25%~40%, 20~40 minutes of cyclohexane volume, to system layering;
7) solution filters, and with the ethanol water washing, spends deionised water again;
8) drying under nitrogen protection, or direct 50 ℃~90 ℃ vacuum drying 2~6 hours.
The present invention adopts reverse micelle method to prepare the PtRu/C catalyst, and this PtRu/C catalyst has high electro catalytic activity to hydrogen and oxygen, methyl alcohol and the oxygen electrochemical reaction of carrying out in the fuel cell especially.Prepared PtRu/C catalyst has that metal carrying capacity height, particle diameter are little, the characteristics of good dispersion and even particle size distribution.As Fig. 1 and Fig. 2 is that (black particles is the PtRu alloying pellet to transmission electron microscope on the photo for Transmission Electron Microscope, the design sketch according to the PtRu/C catalyst of the present invention's preparation that TEM) characterizes.Instrument adopts TECNAIG2F-20 type field, Dutch Philip transmission electron microscope.The PtRu/C catalyst (Fig. 1 and Fig. 2) of the present invention's preparation is measured through energy dispersive spectroscopy (EDS), and the total content of Pt and Ru is respectively 19.4% and 29.65% mass fraction, and the atomic ratio of Pt and Ru was respectively 1: 0.94 and 1: 0.95.Reverse micelle (that is water-in-oil microemulsion) provides a kind of microenvironment, can become the synthetic place (also being called little " reactor ") of desirable nano particle, adopt this method to prepare nano particle, equipment is simple, ambient operation, the metallic particles particle diameter is controlled easily and is distributed more even.
Description of drawings
Fig. 1: embodiment 1PtRu/C catalyst transmission electron microscope picture;
Fig. 2: embodiment 2PtRu/C catalyst transmission electron microscope picture.
The specific embodiment
Embodiment 1
1. dispose chloroplatinic acid (H 2PtCl 6) aqueous solution, its concentration is 0.0386mol/L; Configuration ruthenium trichloride (RuCl 3) aqueous solution, its concentration 0.0765mol/L.
2. dispose cyclohexane, lauryl sodium sulfate and n-octyl alcohol mixed liquor.The mass ratio of lauryl sodium sulfate and cyclohexane is 0.115, with the mass ratio of n-octyl alcohol be 0.7.
3. get 2. mixed liquor 100ml of above-mentioned steps, the mol ratio of water and surfactant is 7, and sonic oscillation 20 minutes drips the 2.19ml chloroplatinic acid and the 1.1ml ruthenium trichloride aqueous solution then respectively.Ultrasonic concussion 30 minutes forms transparent reverse micelle system.
4. in the 3. described system of above-mentioned steps, add carbon black 100mg Vulcan xC-72 carbon black, ultrasonic concussion 20 minutes.
5. add 0.2mol/L potassium borohydride aqueous solution 4.5ml (6 times of theoretical value, water volume 2 times) in the 4. described system of above-mentioned steps, reaction is 20 minutes under the ultrasonic concussion condition, continues to stir to continue reaction 2 hours.
6. add 30ml acetone breakdown of emulsion, ultrasonic oscillation 30 minutes leaves standstill to system layering.
7. solution filters, and uses the absolute ethyl alcohol solution washing, spends deionised water again.
8. 60 ℃ of vacuum drying are 3 hours.
Implementation result is seen accompanying drawing 1.Energy dispersive spectroscopy (EDS) is measured, PtRu total content 19.4% in the catalyst, the atomic ratio of Pt and Ru 1: 0.94.
Embodiment 2
1. dispose chloroplatinic acid (H 2PtCl 6) aqueous solution, its concentration is 0.1mol/L; Configuration ruthenium trichloride (RuCl 3) aqueous solution, its concentration is 0.04mol/L.
2. dispose cyclohexane, lauryl sodium sulfate and n-octyl alcohol mixed liquor.The mass ratio of lauryl sodium sulfate and cyclohexane is 0.078, with the mass ratio of n-octyl alcohol be 1.0.
3. get 2. mixed liquor 130ml of above-mentioned steps, the mol ratio of water and surfactant is 11, and sonic oscillation 15 minutes drips the 1.45ml chloroplatinic acid and the 3.61ml ruthenium trichloride aqueous solution then respectively.Ultrasonic concussion 60 minutes forms transparent reverse micelle system.
4. in the 3. described system of above-mentioned steps, add carbon black 100mg Vulcan XC-72 carbon black, ultrasonic concussion 30 minutes.
5. add 1.5mol/L sodium borohydride aqueous solution 2.53ml (15 times of theoretical value, water volume 0.5 times) in the 4. described system of above-mentioned steps, reaction is 40 minutes under the ultrasonic concussion condition, and mechanical agitation continues reaction 1 hour.
6. add 48ml acetone breakdown of emulsion, ultrasonic oscillation 40 minutes leaves standstill to system layering.
7. solution filters, and with the ethanol water washing, spends deionised water again.
8. 90 ℃ of vacuum drying are 2 hours.
Implementation result is seen accompanying drawing 2.Measure through energy dispersive spectroscopy (EDS), the total content of Pt and Ru is 29.65% mass fraction, and the atomic ratio of Pt and Ru was respectively 1: 0.95.
Embodiment 3
1. dispose chloroplatinic acid (H 2PtCl 6) aqueous solution, its concentration is 0.02mol/L; Configuration ruthenium trichloride (RuCl 3) aqueous solution, its concentration range is 0.20mol/L.
2. dispose cyclohexane, lauryl sodium sulfate and n-octyl alcohol mixed liquor.The mass ratio of lauryl sodium sulfate and cyclohexane is 0.15, with the mass ratio of n-octyl alcohol be 1.2.
3. get 2. mixed liquor 150ml of above-mentioned steps, the mol ratio of water and surfactant is 4.2, and sonic oscillation 40 minutes is distinguished the Dropwise 5 .10ml chloroplatinic acid and the 0.25ml ruthenium trichloride aqueous solution then.Ultrasonic concussion 20 minutes forms transparent reverse micelle system.
4. in the 3. described system of above-mentioned steps, add carbon black 100mg Vulcan xC-72 carbon black, ultrasonic concussion 60 minutes.
5. in the 4. described system of above-mentioned steps, add 0.053mol/L potassium borohydride aqueous solution 8.0ml (3 times of theoretical value, water volume 1.5 times), mechanical agitation successive reaction 1 hour 40 minutes.
6. add 45ml absolute ethyl alcohol breakdown of emulsion, ultrasonic oscillation 20 minutes leaves standstill to system layering.
7. solution filters, and with the ethanol water washing, spends deionised water again.
8. 50 ℃ of vacuum drying are 6 hours.
Implementation result is seen accompanying drawing 2.Measure through energy dispersive spectroscopy (EDS), the total content of Pt and Ru is 19.2% mass fraction, and the atomic ratio of Pt and Ru was respectively 2: 0.91.
The present invention's preparation carbon open and that disclose carries the reverse micelle method of platinum ruthenium (PtRu/C) catalyst, can be by using for reference this paper disclosure.Although method of the present invention is described by preferred embodiment, but those skilled in the art obviously can change method as herein described in not breaking away from content of the present invention, spirit and scope, more particularly, the replacement that all are similar and change apparent to those skilled in the artly, they are regarded as being included in spirit of the present invention, scope and the content.

Claims (1)

1. inverse micelle method for preparing platinum ruthenium/carbon catalyst is characterized in that step is as follows:
1) the configuration concentration scope is 0.02~0.10mol/L chloroplatinic acid aqueous solution, and the configuration concentration scope is 0.04~0.20mol/L ruthenium trichloride aqueous solution, and two kinds of solution constitute water jointly;
2) cyclohexane is an oil phase, and lauryl sodium sulfate is a surfactant, and n-octyl alcohol is a cosurfactant; The mass ratio of lauryl sodium sulfate and cyclohexane and n-octyl alcohol is respectively 0.07~0.15 and 0.5~1.2;
3) above-mentioned steps 2) sonic oscillation or mechanical agitation 15~40 minutes, drip the step 1) water then continuously, the mol ratio of water and surfactant should be 4~11; Ultrasonic concussion 20~60 minutes forms transparent reverse micelle system;
4) in above-mentioned steps 3) add carbon black in the described system, ultrasonic concussion or mechanical agitation 20~60 minutes load on the carbon black reverse micelle;
5) in above-mentioned steps 4) add reducing agent in the described system, reacted 20~40 minutes under mechanical agitation or the ultrasonic oscillation condition, continued stirring reaction 1~2 hour; Reducing agent adopts potassium borohydride or sodium borohydride aqueous solution, and consumption is 3~15 times of theoretical value, and volume is 0.5~2 times of step 3) water volume;
6) stir or the ultrasonic oscillation condition under to add acetone be demulsifier, addition is to leave standstill behind 25%~40%, 20~40 minutes of cyclohexane volume, to system layering;
7) solution filters, and with the ethanol water washing, spends deionised water again;
8) drying under nitrogen protection, or direct 50 ℃~90 ℃ vacuum drying 2~6 hours.
CN200710060188A 2007-12-26 2007-12-26 Reverse micelle method for preparing platinum ruthenium/carbon catalyst Expired - Fee Related CN100588459C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN200710060188A CN100588459C (en) 2007-12-26 2007-12-26 Reverse micelle method for preparing platinum ruthenium/carbon catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN200710060188A CN100588459C (en) 2007-12-26 2007-12-26 Reverse micelle method for preparing platinum ruthenium/carbon catalyst

Publications (2)

Publication Number Publication Date
CN101214437A CN101214437A (en) 2008-07-09
CN100588459C true CN100588459C (en) 2010-02-10

Family

ID=39620979

Family Applications (1)

Application Number Title Priority Date Filing Date
CN200710060188A Expired - Fee Related CN100588459C (en) 2007-12-26 2007-12-26 Reverse micelle method for preparing platinum ruthenium/carbon catalyst

Country Status (1)

Country Link
CN (1) CN100588459C (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4104926A4 (en) * 2020-02-10 2023-08-09 University of Yamanashi Supported metal catalyst, method for producing same, and method for producing carrier

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5715264B2 (en) * 2010-12-29 2015-05-07 オーシャンズ キング ライティング サイエンス アンド テクノロジー シーオー.,エルティーディー Preparation of platinum-ruthenium nanoalloy / graphene catalyst
US20130252138A1 (en) * 2010-12-29 2013-09-26 Ocean's King Lighting Science & Technology Co.,Ltd Pt/graphene catalyst, preparation method and use thereof
CN102989450B (en) * 2012-12-03 2015-03-11 中国科学院大连化学物理研究所 Preparation method, structural feature and application of carrying type nanometer electrocatalyst
CN113070059A (en) * 2021-03-25 2021-07-06 湘潭银河新能源有限公司 Preparation method of platinum-based composite nano electrode catalyst
CN114749172B (en) * 2022-04-21 2023-06-27 清华大学 Continuous preparation method of carbon nanomaterial loaded with small-particle-size noble metal

Non-Patent Citations (6)

* Cited by examiner, † Cited by third party
Title
A new supported catalyst for methanol oxidation prepared bya reverse micelles method. Yicheng Liu, et al.Electrochemistry Communication,Vol.4 . 2002
A new supported catalyst for methanol oxidation prepared bya reverse micelles method. Yicheng Liu,et al.Electrochemistry Communication,Vol.4. 2002 *
A review of anode catalysis in the direct methanol fuel cell. Hansan Liu, et al.Journal of Power Sources,Vol.155 . 2006
A review of anode catalysis in the direct methanol fuel cell. Hansan Liu,et al.Journal of Power Sources,Vol.155. 2006 *
Catalytic activity of Pt-Ru alloys synthesized by amicroemulsion method in direct methanol fuel cells. L. Xiong, A. Manthiram.Solid State Ionic,Vol.176 . 2005
Catalytic activity of Pt-Ru alloys synthesized by amicroemulsion method in direct methanol fuel cells.L.Xiong,A.Manthiram.Solid State Ionic,Vol.176. 2005 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4104926A4 (en) * 2020-02-10 2023-08-09 University of Yamanashi Supported metal catalyst, method for producing same, and method for producing carrier

Also Published As

Publication number Publication date
CN101214437A (en) 2008-07-09

Similar Documents

Publication Publication Date Title
Wang et al. Effect of Ni on PtRu/C catalyst performance for ethanol electrooxidation in acidic medium
Fichtner et al. Top-Down Synthesis of Nanostructured Platinum–Lanthanide Alloy Oxygen Reduction Reaction Catalysts: Pt x Pr/C as an Example
Brouzgou et al. PEMFCs and AEMFCs directly fed with ethanol: a current status comparative review
CN101157033B (en) A mesoporous Pt/WO3 electro-catalyst and its preparing method
CN100488633C (en) Carbon-carried platinum-based catalyst for fuel cell and its preparation method
Li et al. A novel anode for direct borohydride-hydrogen peroxide fuel cell: Au nanoparticles decorated 3D self-supported reduced graphene oxide foam
Wang et al. Carbon supported Ag nanoparticles with different particle size as cathode catalysts for anion exchange membrane direct glycerol fuel cells
CN100588459C (en) Reverse micelle method for preparing platinum ruthenium/carbon catalyst
CN101780414B (en) PtRuNi/C ternary alloy nanometer catalyst and preparation method thereof
CN101380594A (en) Titanium nitride carrier of catalyst of fuel batter with proton exchange film or titanium nitride and carbon carrier mixing carrier
Kadioglu et al. Investigation of the performance of a direct borohydride fuel cell with low Pt/C catalyst loading under different operating conditions
CN108155392A (en) A kind of preparation method of redox graphene load Pd-M nano-composite catalysts
CN101773839B (en) PtRuCo/C ternary alloy nano catalyst and preparation method thereof
Lee et al. Electrocatalytic activity and durability study of carbon supported Pt nanodendrites in polymer electrolyte membrane fuel cells
Nbelayim et al. Preparation and characterization of stable and active Pt@ TiO2 Core–shell nanoparticles as electrocatalyst for application in PEMFCs
CN103706375B (en) Preparation method for the PtFe/C catalyst of Proton Exchange Membrane Fuel Cells
Li et al. Ultrathin metallic nanowire-based architectures as high-performing electrocatalysts
CN101286564A (en) Composite anode for direct methanol fuel cell and method for making the same
Dickinson et al. Performance of methanol oxidation catalysts with varying Pt: Ru ratio as a function of temperature
CN103401000B (en) Used in proton exchange membrane fuel cell catalyst, its preparation method and Proton Exchange Membrane Fuel Cells
CN101580225B (en) Method for preparing low platinum modified carbon-loaded ruthenium nano particles and application thereof
CN108746659B (en) Flower-shaped AgPd nano alloy and preparation and use methods thereof
JP2006252797A (en) Manufacturing method of oxygen electrode catalyst for fuel cell, and of direct methanol fuel cell and catalyst
CN101752571A (en) Anode catalyst of direct methanol fuel cell and preparation method thereof
CN109876800A (en) A kind of preparation method preparing platinum/carbon nano catalyst

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20100210

Termination date: 20111226