CN106784879B - A kind of preparation method of the palladium ruthenium catalyst of titanium plate load - Google Patents

A kind of preparation method of the palladium ruthenium catalyst of titanium plate load Download PDF

Info

Publication number
CN106784879B
CN106784879B CN201710032037.6A CN201710032037A CN106784879B CN 106784879 B CN106784879 B CN 106784879B CN 201710032037 A CN201710032037 A CN 201710032037A CN 106784879 B CN106784879 B CN 106784879B
Authority
CN
China
Prior art keywords
palladium
titanium plate
ruthenium
preparation
plate load
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
CN201710032037.6A
Other languages
Chinese (zh)
Other versions
CN106784879A (en
Inventor
张腾
张心愿
魏颖
李巍婷
温翠莲
唐电
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.)
Fuzhou University
Original Assignee
Fuzhou 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 Fuzhou University filed Critical Fuzhou University
Priority to CN201710032037.6A priority Critical patent/CN106784879B/en
Publication of CN106784879A publication Critical patent/CN106784879A/en
Application granted granted Critical
Publication of CN106784879B publication Critical patent/CN106784879B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/88Processes of manufacture
    • H01M4/8803Supports for the deposition of the catalytic active composition
    • HELECTRICITY
    • H01ELECTRIC ELEMENTS
    • H01MPROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M4/00Electrodes
    • H01M4/86Inert electrodes with catalytic activity, e.g. for fuel cells
    • H01M4/90Selection of catalytic material
    • H01M4/9041Metals or alloys
    • 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

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses a kind of preparation methods of the palladium ruthenium catalyst of titanium plate load; it is using titanium plate as carrier; using palladium salt and ruthenium salt as presoma; oleic acid is added or oleate forms jelly; then jelly is uniformly coated in titanium plate; isothermal holding 0.5h ~ 2h under 160 ~ 320 DEG C, protective gas obtains the palladium ruthenium nanocatalyst of titanium plate load.Compared with traditional thermolysis process, the method of the present invention can significantly reduce thermal decomposition temperature, make the palladium ruthenium particle size uniformity obtained, average grain diameter is in 10nm or less, and palladium ruthenium can be made evenly dispersed in titanium plate, to realize the higher catalytic activity to Aalcohols fuels such as ethyl alcohol and methanol.Raw material of the present invention is easy to get, and operating method is easy, can reach the requirement of industrialization production.

Description

A kind of preparation method of the palladium ruthenium catalyst of titanium plate load
Technical field
The invention belongs to be catalyzed and energy industry material preparation field, and in particular to a kind of palladium ruthenium nanometer of titanium plate load is urged The preparation method of agent.
Background technique
With the aggravation of global energy crisis, the new energy causes the extensive concern of society.Direct alcohol fuel cell (DMFCs/DEFCs) it is a kind of electrochemical reaction appts that the chemical energy of fuel can be directly changed into electric energy, there is work Temperature is low, energy density is high and advantages of environment protection.In terms of fuel cell, the catalytic efficiency of platinum catalyst is higher, but It is the scarcity of resources of noble metal platinum, leads to that it is expensive, increases the cost of fuel cell.Therefore, palladium is considered as low platinum Or even the critical material without platinum catalyst.
However, traditional carbon material carrier causes during as catalyst carrier thereon because its corrosion resistance is poor The catalyst activity substance of load is easy to fall off, influences its catalytic performance.In recent years, numerous studies personnel to non-carbon support material such as Oxide, high stability metal and rare earth material etc. are studied.Wherein, titanium electric conductivity with higher and corrosion-resistant, can Hope the novel carriers material for becoming fuel cell.
Summary of the invention
The purpose of the present invention is to provide a kind of preparation methods of the palladium ruthenium nanocatalyst of titanium plate load, can make to be made Palladium ruthenium grain diameter it is uniform, and be dispersed in it on carrier, to significantly improve the catalytic activity of gained catalyst.
To achieve the above object, the present invention adopts the following technical scheme:
A kind of preparation method of the palladium ruthenium catalyst of titanium plate load, is to be dissolved in palladium salt under ultrasonic agitation with ruthenium salt In organic solvent, solution A is obtained;By oleic acid or oleate ultrasonic dissolution in organic solvent, solution B is obtained;Dropwise by solution A It is added in solution B, is stirred 1h ~ 4h, obtains colloidal solution C;In titanium plate after colloidal solution C to be evenly applied to etching, It is dried to obtain substance D;Substance D is transferred in tube furnace, isothermal holding 0.5h after 160 ~ 320 DEG C are warming up under gas shield ~ 2h obtains the palladium ruthenium catalyst of titanium plate load;Itself specific steps are as follows:
(1) titanium plate is etched 1-2 hours in the oxalic acid solution of 20wt% ~ 60wt% of boiling, after washing is dry, is carved Titanium plate after erosion;
(2) by mass volume ratio 1:1:10 by palladium salt, ruthenium salt ultrasonic mixing in organic solution, obtain solution A;By quality Oleic acid or oleate ultrasonic dissolution in organic solvent, are obtained solution B by volume ratio 1:10;
(3) agitating solution B, and solution A is added dropwise in solution B, it is then stirred 1h ~ 4h, obtains glue Solution C;
(4) it in the titanium plate after colloidal solution C to be evenly coated in etching, is put into drying box, dry 2h, obtains object at 60 DEG C Matter D;
(5) substance D is put into corundum ceramic boat, is transferred in tube furnace, be passed through protective gas, then with 2 DEG C/min Rate be warming up to 160 DEG C ~ 320 DEG C, isothermal holding 0.5h ~ 2h, the palladium ruthenium catalyst of titanium plate load is obtained after cooling.
The palladium salt is one of palladium chloride, sodium tetrachloropallate and palladium acetate or several.
The ruthenium salt is one of ruthenium trichloride, acetic acid ruthenium and iodate ruthenium or several.
The oleate is one of potassium oleate, calcium oleate and enuatrol or several.
The organic solvent is dehydrated alcohol or ethylene glycol.
Protective gas used is the one or several kinds of argon gas, hydrogen, nitrogen.
The molar ratio of palladium salt, ruthenium salt and oleic acid or oleate used is 1:1:1 ~ 1:1:10.
Coated weight of the colloidal solution C in titanium plate is 1 ~ 10g/m2
Palladium in gained catalyst, ruthenium particle average grain diameter be respectively less than 10nm.
Remarkable advantage of the invention is:
Compared with traditional thermolysis process, the method for the present invention can not only significantly reduce thermal decomposition temperature, make the palladium ruthenium obtained Particle size uniformity, average grain diameter is less than 10nm, and palladium ruthenium particle can be made evenly dispersed in titanium plate, to give full play to the conjunction of palladium ruthenium The Lattice Contraction effect and surface coordination effect of gold, thus to the Aalcohols fuels such as ethyl alcohol and methanol catalytic activity with higher. Meanwhile the high corrosion-resistant of titanium-based material can also enhance the stability of catalyst under the runtime environment.
Raw material of the present invention is easy to get, and operating method is easy, can reach the requirement of industrialization production.
Detailed description of the invention
Fig. 1 is the SEM figure of the palladium ruthenium catalyst of titanium plate load prepared by the present invention.
Specific embodiment
In order to make content of the present invention easily facilitate understanding, With reference to embodiment to of the present invention Technical solution is described further, but the present invention is not limited only to this.
Embodiment 1
(1) titanium plate is etched 1 hour in the oxalic acid solution of the 60wt% of boiling, after ethanol wash drying, is etched Titanium plate afterwards;
(2) by palladium acetate and iodate ruthenium ultrasonic mixing in dehydrated alcohol, obtaining palladium acetate and iodate ruthenium concentration is 1g/ The solution A of 10mL;By oleic acid ultrasonic dissolution in dehydrated alcohol, the solution B that concentration is 1g/10mL is obtained;
(3) agitating solution B, and solution A is added dropwise in solution B, it is then stirred 1h, obtains colloidal solution C;Wherein oleic acid and palladium acetate, the molar ratio of iodate ruthenium are 1:1:1;
(4) coated weight 1g/m is pressed2In titanium plate after colloidal solution C to be evenly coated in etching, it is put into drying box, at 60 DEG C Dry 2h, obtains substance D;
(5) substance D is put into corundum ceramic boat, is transferred in tube furnace, be passed through argon gas and protected, then with 2 DEG C/ The rate of min is warming up to 160 DEG C, isothermal holding 2h, and the palladium ruthenium catalyst of titanium plate load is obtained after cooling.Gained catalyst is to second The specific activity of alcohol catalysis is 25 mAcm-2, the attenuation rate of continuous operation 12 hours (65 DEG C of 10.65V) is only 10%.
Fig. 1 is the SEM figure of gained catalyst.As seen from the figure, palladium ruthenium nano-particle is uniformly dispersed, and average grain diameter is in 10nm Left and right.
Embodiment 2
(1) titanium plate is etched 1 hour in the oxalic acid solution of the 40wt% of boiling, after ethanol wash drying, is etched Titanium plate afterwards;
(2) it by palladium chloride and ruthenium trichloride ultrasonic mixing in dehydrated alcohol, obtains palladium chloride and ruthenium trichloride is dense Degree is the solution A of 1g/10mL;By potassium oleate ultrasonic dissolution in ethylene glycol, the solution B that concentration is 1g/10mL is obtained;
(3) agitating solution B, and solution A is added dropwise in solution B, it is then stirred 2h, obtains colloidal solution C;Wherein the molar ratio of potassium oleate and palladium chloride, ruthenium trichloride is 10:1:1;
(4) coated weight 10g/m is pressed2In titanium plate after colloidal solution C to be evenly coated in etching, it is put into drying box, 60 DEG C Lower dry 2h, obtains substance D;
(5) substance D is put into corundum ceramic boat, is transferred in tube furnace, be passed through nitrogen and protected, then with 2 DEG C/ The rate of min is warming up to 320 DEG C, isothermal holding 0.5h, and the palladium ruthenium catalyst of titanium plate load is obtained after cooling.Gained catalyst pair The specific activity of alcohol catalysis is 20 mAcm-2, the attenuation rate of continuous operation 12 hours (65 DEG C, 0.65V) is only 8%.
Embodiment 3
(1) titanium plate is etched 2 hours in the oxalic acid solution of the 20wt% of boiling, after ethanol wash drying, is etched Titanium plate afterwards;
(2) by palladium acetate and acetic acid ruthenium ultrasonic mixing in ethylene glycol, obtaining palladium acetate and acetic acid ruthenium concentration is 1g/ The solution A of 10mL;By enuatrol ultrasonic dissolution in ethylene glycol, the solution B that concentration is 1g/10mL is obtained;
(3) agitating solution B, and solution A is added dropwise in solution B, it is then stirred 4h, obtains colloidal solution C;Wherein enuatrol and palladium acetate, the molar ratio of acetic acid ruthenium are 5:1:1;
(4) coated weight 5g/m is pressed2In titanium plate after colloidal solution C to be evenly coated in etching, it is put into drying box, at 60 DEG C Dry 2h, obtains substance D;
(5) substance D is put into corundum ceramic boat, is transferred in tube furnace, argon gas progress is passed through, then with 2 DEG C/min Rate be warming up to 180 DEG C, isothermal holding 1h, the palladium ruthenium catalyst of titanium plate load is obtained after cooling.Gained catalyst is to ethyl alcohol The specific activity of catalysis is 14 mAcm-2, the attenuation rate of continuous operation 12 hours (65 DEG C, 0.65V) is only 5%.
The foregoing is merely presently preferred embodiments of the present invention, all equivalent changes done according to scope of the present invention patent with Modification, is all covered by the present invention.

Claims (7)

1. a kind of preparation method of the palladium ruthenium catalyst of titanium plate load, it is characterised in that: by palladium salt and ruthenium salt under ultrasonic agitation It is dissolved in organic solvent, obtains solution A;By oleic acid or oleate ultrasonic dissolution in organic solvent, solution B is obtained;It will be molten Liquid A is added dropwise in solution B, is stirred 1h ~ 4h, obtains colloidal solution C;After colloidal solution C is evenly applied to etching In titanium plate, it is dried to obtain substance D;Substance D is transferred in tube furnace, is kept the temperature after 160 ~ 320 DEG C are warming up under gas shield 0.5h ~ 2h is handled, the palladium ruthenium catalyst of titanium plate load is obtained;
The molar ratio of palladium salt, ruthenium salt and oleic acid or oleate used is 1:1:1 ~ 1:1:10;
Coated weight of the colloidal solution C in titanium plate is 1 ~ 10g/m2
2. the preparation method of the palladium ruthenium catalyst of titanium plate load according to claim 1, it is characterised in that: the palladium salt is two One of palladium chloride, sodium tetrachloropallate and palladium acetate are several.
3. the preparation method of the palladium ruthenium catalyst of titanium plate load according to claim 1, it is characterised in that: the ruthenium salt is three One of ruthenic chloride, acetic acid ruthenium and iodate ruthenium are several.
4. the preparation method of the palladium ruthenium catalyst of titanium plate load according to claim 1, it is characterised in that: the oleate is One of potassium oleate, calcium oleate and enuatrol are several.
5. the preparation method of the palladium ruthenium catalyst of titanium plate load according to claim 1, it is characterised in that: the organic solvent For dehydrated alcohol or ethylene glycol.
6. the preparation method of the palladium ruthenium catalyst of titanium plate load according to claim 1, it is characterised in that: protective gas used For the one or several kinds of argon gas, hydrogen, nitrogen.
7. the preparation method of the palladium ruthenium catalyst of titanium plate load according to claim 1, it is characterised in that: in gained catalyst Palladium, ruthenium particle average grain diameter be respectively less than 10nm.
CN201710032037.6A 2017-01-17 2017-01-17 A kind of preparation method of the palladium ruthenium catalyst of titanium plate load Expired - Fee Related CN106784879B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201710032037.6A CN106784879B (en) 2017-01-17 2017-01-17 A kind of preparation method of the palladium ruthenium catalyst of titanium plate load

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201710032037.6A CN106784879B (en) 2017-01-17 2017-01-17 A kind of preparation method of the palladium ruthenium catalyst of titanium plate load

Publications (2)

Publication Number Publication Date
CN106784879A CN106784879A (en) 2017-05-31
CN106784879B true CN106784879B (en) 2019-09-13

Family

ID=58946141

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201710032037.6A Expired - Fee Related CN106784879B (en) 2017-01-17 2017-01-17 A kind of preparation method of the palladium ruthenium catalyst of titanium plate load

Country Status (1)

Country Link
CN (1) CN106784879B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN115365508B (en) * 2022-09-09 2023-06-20 安徽吉华新材料有限公司 Preparation method of ruthenium-titanium intermetallic compound nano-particles

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102698745A (en) * 2012-06-06 2012-10-03 厦门大学 Titanium dioxide nanotube carried palladium nano catalyst and preparation method of same

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001224963A (en) * 2000-02-16 2001-08-21 Nissan Motor Co Ltd Catalytic composition, its manufacturing method and its using method

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102698745A (en) * 2012-06-06 2012-10-03 厦门大学 Titanium dioxide nanotube carried palladium nano catalyst and preparation method of same

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
"直接甲酸燃料电池阳极Pd基催化剂的性能研究";孙丹丹;《中国优秀硕士学位论文全文数据库》;20160216;第C042-1628页 *

Also Published As

Publication number Publication date
CN106784879A (en) 2017-05-31

Similar Documents

Publication Publication Date Title
CN105170169B (en) A kind of nitrogen-doped graphene iron-based nano-particles reinforcement type catalyst and preparation method thereof
CN103495432B (en) A kind of fuel-cell catalyst preparation method of efficient stable
CN105529472B (en) Flake porous two-dimentional carbon material of a kind of Co-N codope and preparation method thereof
CN105244513A (en) Graphite-phase carbon nitride-modified carbon black-loaded platinum-palladium alloy nano electrocatalyst and preparation method
CN106784897B (en) A kind of preparation method of anode of fuel cell Pd/CNTs nanocatalyst
CN113764688B (en) Three-dimensional carbon structure supported GaN catalyst and preparation method thereof
CN106410224A (en) Cobalt-carbon porous nanocomposite oxygen reduction electrocatalyst and its preparation method and application
CN103022521A (en) Palladium-cobalt/graphene nano electro-catalyst and preparation method thereof
CN102723504A (en) Multi-wall carbon nano-tube carried core-shell silver-platinum cathode catalyst and preparation method
CN106925314A (en) A kind of nickel assisted cryogenic synthesizes the method for molybdenum carbide elctro-catalyst
CN104505523B (en) Platinum-based catalyst/graphene composite material and preparation method thereof
Wang et al. Chemical induced fragmentation of MOFs for highly efficient Ni-based hydrogen evolution catalysts
CN109482214A (en) The catalyst and preparation method of a kind of graphene-supported ruthenium metal and application
CN105810960B (en) It is a kind of using nickel foam as the composite material and preparation method of matrix
CN110961162A (en) Catalyst carrier, precious metal catalyst, and preparation method and application thereof
CN103831103A (en) Graphene aerogel catalyst and preparation method thereof
CN103816894A (en) Pt-Ru alloy nano electro-catalyst having doped graphene carrier and preparation method thereof
CN102983339A (en) Platinum-cobalt/graphene nano electrocatalyst and preparation method thereof
CN104151821B (en) A kind of preparation of the flower-shaped porous carbon material composite being applied to fuel cell catalyst
CN110548507B (en) Preparation method of carbon-supported nano-silver catalyst
CN105435780A (en) Nano platinum-ruthenium alloy supporting nitrogen-doped graphene catalyst
CN106784879B (en) A kind of preparation method of the palladium ruthenium catalyst of titanium plate load
CN113258085A (en) Oxygen-containing silicon nanosheet supported noble metal catalyst and preparation method and application thereof
CN107946606A (en) Nitrogen co-doped mesoporous carbon fiber of iron and preparation method thereof and apply in a fuel cell
CN106602085B (en) A kind of preparation method of anode of fuel cell palladium ruthenium nanocatalyst

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20190913

Termination date: 20220117

CF01 Termination of patent right due to non-payment of annual fee