CN102806079A - Preparation method of Pd/SnO2/C composite nanometer catalyst - Google Patents
Preparation method of Pd/SnO2/C composite nanometer catalyst Download PDFInfo
- Publication number
- CN102806079A CN102806079A CN2012102894029A CN201210289402A CN102806079A CN 102806079 A CN102806079 A CN 102806079A CN 2012102894029 A CN2012102894029 A CN 2012102894029A CN 201210289402 A CN201210289402 A CN 201210289402A CN 102806079 A CN102806079 A CN 102806079A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- sno
- preparation
- nano
- vulcan
- 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.)
- Granted
Links
Images
Landscapes
- Catalysts (AREA)
Abstract
The invention relates to a preparation method of a Pd/SnO2/C composite nanometer catalyst. According to the preparation method, SnO2 nanometer particles are prepared by a hydrothermal method, Vulcan XC-72 active carbon powder and the SnO2 nanometer particles are fully and uniformly mixed in mixed solution of glycol and deionized water, a liquid phase reduction method is used for loading nanometer Pd particles, finally, the suction filtration and the drying are carried out, and the Pd/SnO2/C composite nanometer catalyst is obtained. Compared with the prior art, the preparation has the advantages that SnO2 is introduced into a Pd catalyst system catalyzed and oxidized by ethanol, the Pd/SnO2/C composite nanometer catalyst is prepared, and the catalyst has high catalytic activity on ethanol oxidation reaction.
Description
Technical field
The invention belongs to the nano-catalyst material preparing technical field, especially relate to a kind of Pd/SnO
2The preparation method of/C composite nano-catalyst.
Background technology
Directly the alcohols battery (fuel cell FC) is a kind of emerging electrochmical power source, it with the chemical energy of fuel be converted into electric energy, do not receive the restriction of Carnot cycle, energy conversion efficiency is high; Product has been got rid of NOx, SO basically
XDeng the influence of polluter, has environmental friendliness; Specific power is high; Characteristics such as specific energy height.Yet in realizing the commercialization process, also there are a lot of technology, economic headache.
At present Pt is catalyst based better to alcohols catalytic oxidation effect, but is fuel for adopting methyl alcohol, and the intermediate product of methanol oxidation can be strong is adsorbed on the Pt surface; Cause catalyst poisoning; Catalytic performance fails very soon, and Pt costs an arm and a leg, and reserves are limited.Pd is considered to one of important substitution material.Pd content in the earth's crust is abundanter, and relative price is cheap, and under alkali condition, ethanol is had better catalytic activity.
Be further to improve the catalytic activity of catalyst, reduce catalyst consumption, can improve fuel cell performance from two aspects: the one, prepare the catalyst of highly active polymolecularity, two are to use the porous carrier of high specific area.Present research is illustrated in and adds different metal or oxide on the Pd catalyst basis, is prepared into Pd base binary or multicomponent catalyst and can significantly improves the catalytic activity to ethanol.T.Maiyalagan has introduced second kind of metal Ni, has prepared the Pd-Ni/C catalyst, and with respect to Pd/C, when oxidation ethanol, the initial oxidation current potential is negative to move 200mv, and peak current density is four times of Pd/C.R.Mmalewane has prepared Pd-Sn/C and two kinds of catalyst of Pd-Ru-Sn/C; The binary metal catalyst that wherein only contains metal Sn has better catalytic activity of pair ethanol and anti-CO poisoning capability in alkaline solution; And catalytic activity is significantly improved than Pd/C after adding Sn; In the XRD figure sheet of Pd-Sn/C, there are Pd and SnO
2The crystal peak.C.Mahendiran adds oxide NiO/MgO in the Pd catalyst, the Pd/ of preparation (NiO/MgOC) catalyst, and it has active and stable preferably in alkaline solution to oxidation of ethanol.In fuel-cell catalyst, add SnO
2, have clear improvement for improving catalytic activity and the anti-CO poisoning capability of catalyst.
Summary of the invention
The object of the invention is exactly for the defective that overcomes above-mentioned prior art existence a kind of Pd/SnO that the oxidation of ethanol reaction is had very high catalytic activity to be provided
2The preparation method of/C composite nano-catalyst.
The object of the invention can be realized through following technical scheme:
A kind of Pd/SnO
2The preparation method of/C composite nano-catalyst may further comprise the steps:
(1) Hydrothermal Preparation SnO
2Nano particle;
A, Macrogol 2000 (PEG2000) is dissolved in the absolute ethyl alcohol, adds SnCl again after the dissolving fully
22H
2O forms mixed solution, 50 ℃ of temperature controls reaction 2h under the magnetic agitation, ageing 12h at room temperature then;
B, in autoclave, carry out high-temperature high-voltage reaction, filtering drying obtains pale yellow powder and is SnO
2Nano particle;
(2) with Vulcan XC-72 activated carbon powder and SnO
2The nano particle mass ratio is that mixing in 1: 1 is placed in the mixed solvent of ethylene glycol and deionized water composition Vulcan XC-72 activated carbon powder and SnO
2The addition of nano particle is the 40mg/120ml mixed solvent, and the control temperature is 60 ℃, utilizes powerful stirring of magnetic stirring apparatus fully to mix;
(3) with liquid phase reduction loaded with nano Pd particle:
The PdCl that in the mixed liquor that step (2) obtains, dropwise adds 2mmol/L
2Solution stirred after one hour, and the trisodium citrate that adding contains two crystallizations water is as stabilizing agent; The mol ratio of control metal Pd and trisodium citrate is 1: 5, and ultrasonic concussion 30min mixes; With the pH value to 11 of alkaline solution NaOH regulator solution, add reducing agent then again, continue isothermal reaction 3h; Be cooled to room temperature then, filtering to wash to filter cake does not have Cl-, and vacuum drying 12h promptly obtains the Pd/SnO of black
2/ C catalyst.
In the mixed solution described in the step (1), the concentration of Macrogol 2000 is 0.004-0.005g/ml, SnCl
2Concentration be 0.04-0.05g/ml.
Vulcan XC-72 activated carbon powder described in the step (2) through preliminary treatment, may further comprise the steps before mixing: the control temperature is 90 ℃, with the HNO of active carbon Vulcan XC-72 at 5mol/L
3In the powerful 5h that stirs, filter and washing after being cooled to room temperature; Control temperature again at 130 ℃ of vacuum drying 6h, grinding the active carbon after handling also, 200 mesh sieve branches obtain even-grained Vulcan XC-72 activated carbon powder.
The volume ratio of ethylene glycol described in the step (2) and deionized water is 1: 3.
Reducing agent described in the step (3) is a sodium borohydride.
Pd/SnO described in the step (3)
2The load capacity of nanometer Pd particle is 20wt% in the/C catalyst.
Compared with prior art, the present invention considers that in alkaline environment Pd has the activity higher than Pt to the catalytic oxidation of ethanol, in acid, alkaline media, good stability is arranged all, is a kind of eelctro-catalyst and catalyst carrier of function admirable, SnO
2Good electro-chemical activity is arranged, and hydrothermal stability is SnO
2Be incorporated into the Pd catalyst system of alcohol catalysis oxidation, be prepared into Pd/SnO
2/ C composite nano-catalyst, this catalyst has very high catalytic activity to the oxidation of ethanol reaction.
Description of drawings
Fig. 1 is Pd/SnO
2/ C composite nano-catalyst and/SnO
2TEM figure.
Fig. 2 is Pd/SnO
2/ C composite nano-catalyst and SnO
2XRD figure.
Fig. 3 is Pd/SnO
2The stripping volt-ampere curve of/C composite nano-catalyst in 1molL-1KOH solution.Analysing of hydrogen occurred and attached the peak, shown that catalyst has the certain activity specific area.
Fig. 4 is Pd/C catalyst and Pd/SnO
2/ C composite nano-catalyst is respectively at 0.1mol/LCH
3CH
2Cyclic voltammetry curve in OH and the 0.1mol/L KOH solution.
Fig. 5 is Pd/C catalyst and Pd/SnO
2/ C composite nano-catalyst is at 1M KOH+1M C
2H
5Time current curve among the OH.
The specific embodiment
Below in conjunction with accompanying drawing and specific embodiment the present invention is elaborated.
X-ray powder diffraction instrument is German Bruker D8-ADVANCE type, and radiation source is that (per step stops 1s to CuK α for λ=0.15418nm), 0.0167 ° of step-length, and sweep limits is 20~90 °; The Shanghai occasion China CHI660C of instrument company electrochemical workstation; Palladium bichloride (PdCl
2, Shanghai fine chemistry industry Materials Research Laboratories is analyzed pure); Vulcan XC-72 (U.S. Cabot company, 98%); Ethanol (Chinasun Specialty Products Co., Ltd analyzes pure); Ethylene glycol (Chemical Reagent Co., Ltd., Sinopharm Group analyzes pure); NaOH (chemical reagent Co., Ltd in Shanghai analyzes pure); Nafion solution (5 (wt) %, U.S. DuPont company).
Embodiment 1
The preparation of 1 composite catalyst:
Hydrothermal Preparation SnO
2Nano particle is 1: 1 according to mass ratio then, pretreated VulcanXC-72 activated carbon powder of process and SnO
2Nano particle fully mixes in ethylene glycol and deionized water (volume ratio is 1: 3) solution, and magnetic stirring apparatus is powerful to be stirred.With liquid phase reduction loaded with nano Pd particle, load capacity is wt.20%, in the reduction process, needs to add certain amount of stabilizer, and trisodium citrate drips excessive borane reducing agent sodium hydride, and after reaction a period of time, through filtering, oven dry obtains Pd/SnO
2/ C composite nano-catalyst.This catalyst has very high catalytic activity to the oxidation reaction of ethanol.
Fig. 1 is Pd/SnO
2/ C composite nano-catalyst and/SnO
2TEM figure, utilize transmission electron microscope to Pd/SnO
2/ C nanocatalyst scans, and the TEM picture of gained is as shown in Figure 1, from Fig. 1, can clearly find out finely dispersed Pd nano particle, and particle diameter is about 3-5nm.Fig. 2 is Pd/SnO
2/ C composite nano-catalyst and SnO
2XRD figure, from SnO
2XRD figure, with SnO
2Standard card (JCPDS No.41-1445) relatively, can find out SnO
2Characteristic diffraction peak 2 θ=26.6 ° (110), 33.9 ° (101), 51.8 ° (211), 64.7 ° (112); Contrast Pd/SnO
2The XRD figure of/C composite nano-catalyst, but the diffraction maximum of SnO2 has skew offset amplitude to a certain degree little.In the XRD figure of composite catalyst, (JCPDS, No.46-1043) relatively, 40.1 °, 46.7 °, 82.0 ° of the diffraction maximums of Pd are respectively 111,200,311 crystal faces of Pd with the accurate card of the change of Pd.
The preparation of 2 catalysis electrodes:
Take by weighing the catalyst of a certain amount of above-mentioned preparation, measure deionized water, ethanol, 5%Nafion solution by a certain percentage, catalyst and mixed solution is mixed; Ultrasonic concussion 30min; Obtain the watery catalyst of black ink, measure a certain amount of ink, be overlying on the glass-carbon electrode surface with pipette; Naturally after drying, electrode completes.Working electrode is glass carbon (GC) electrode (d=3mm), uses preceding Al with 0.3 μ m
2O
3Powder is milled to minute surface on chamois leather, spend the supersound washing of ionic hydration absolute ethyl alcohol more respectively.
3 catalytic properties characterize:
As working electrode, is reference electrode with SCE with the electrode for preparing, and the Pt electrode carries out cyclic voltammetric test and the test of time current curve for electrode is formed three electrode test systems on CHI660C.
Fig. 3 is Pd/SnO
2/ C composite nano-catalyst is at 1molL
-1Stripping volt-ampere curve in the KOH solution analysing of hydrogen occurred and has attached the peak, shows that catalyst has the certain activity specific area.Fig. 4 is Pd/C catalyst and Pd/SnO
2/ C composite nano-catalyst is respectively at 0.1mol/LCH
3CH
2Cyclic voltammetry curve in OH and the 0.1mol/LKOH solution.On scheming, can find out Pd/SnO
2The catalytic performance of/C composite nano-catalyst is higher than Pd/C catalyst, Pd/SnO far away
2/ C composite nano-catalyst under very low current potential, is about-0.4V (vs.SCE) in just inswept journey, ethanol just begins to take place catalytic oxidation, when-0.25V, reaches maximum, the about 60mA/cm of its peak current density
2During reverse scan, because of catalyst P d changes active Pd atom again into, again above that ethanol of absorption is carried out catalytic oxidation, its oxidation peak reaches maximum at-0.42V, and catalytic current reaches 58mA/cm
2Fig. 5 is Pd/C catalyst and Pd/SnO
2/ C composite nano-catalyst is at 1M KOH+1M C
2H
5Time current curve among the OH.Prolong in time, current attenuation, but attenuation amplitude is little, explains that the anti-CO poisoning capability of composite catalyst is relatively good, contrasts two groups of data and can find out Pd/SnO
2It is littler than Pd/C that the current density of/C composite nano-catalyst reduces amplitude, and this explanation adds SnO
2Better anti-CO poisoning capability is arranged.
Embodiment 2
A kind of Pd/SnO
2The preparation method of/C composite nano-catalyst may further comprise the steps:
(1) Hydrothermal Preparation SnO
2Nano particle:
A, Macrogol 2000 (PEG2000) is dissolved in the absolute ethyl alcohol, adds SnCl again after the dissolving fully
22H
2O forms mixed solution, and the concentration of Macrogol 2000 is 0.004g/ml in the mixed solution, SnCl
2Concentration be 0.04g/ml, 50 ℃ of temperature controls reaction 2h under the magnetic agitation, ageing 12h at room temperature then;
B, in autoclave, carry out high-temperature high-voltage reaction, filtering drying obtains pale yellow powder and is SnO
2Nano particle;
(2) with Vulcan XC-72 activated carbon powder and SnO
2The nano particle mass ratio is that mixing in 1: 1 is placed in the mixed solvent of ethylene glycol and deionized water (volume ratio is 1: 3) composition Vulcan XC-72 activated carbon powder and SnO
2The addition of nano particle is the 40mg/120ml mixed solvent, and the control temperature is 60 ℃, utilizes powerful stirring of magnetic stirring apparatus fully to mix;
(3) with liquid phase reduction loaded with nano Pd particle:
The PdCl that in the mixed liquor that step (2) obtains, dropwise adds 2mmol/L
2Solution stirred after one hour, and the trisodium citrate that adding contains two crystallizations water is as stabilizing agent; The mol ratio of control metal Pd and trisodium citrate is 1: 5, and ultrasonic concussion 30min mixes; With the pH value to 11 of alkaline solution NaOH regulator solution, add the borane reducing agent sodium hydride then again, continue isothermal reaction 3h; Be cooled to room temperature then, filtering to wash to filter cake does not have Cl
-, vacuum drying 12h promptly obtains the Pd/SnO of black
2/ C catalyst, the load capacity of nanometer Pd particle are 20wt%.
Wherein, Vulcan XC-72 activated carbon powder through preliminary treatment, may further comprise the steps before mixing: the control temperature is 90 ℃, with the HNO of active carbon Vulcan XC-72 at 5mol/L
3In the powerful 5h that stirs, filter and washing after being cooled to room temperature; Control temperature again at 130 ℃ of vacuum drying 6h, grinding the active carbon after handling also, 200 mesh sieve branches obtain even-grained Vulcan XC-72 activated carbon powder.
Embodiment 3
A kind of Pd/SnO
2The preparation method of/C composite nano-catalyst may further comprise the steps:
(1) Hydrothermal Preparation SnO
2Nano particle:
A, Macrogol 2000 (PEG2000) is dissolved in the absolute ethyl alcohol, adds SnCl again after the dissolving fully
22H
2O forms mixed solution, and the concentration of Macrogol 2000 is 0.005g/ml in the mixed solution, SnCl
2Concentration be 0.05g/ml, 50 ℃ of temperature controls reaction 2h under the magnetic agitation, ageing 12h at room temperature then;
B, in autoclave, carry out high-temperature high-voltage reaction, filtering drying obtains pale yellow powder and is SnO
2Nano particle;
(2) with Vulcan XC-72 activated carbon powder and SnO
2The nano particle mass ratio is that mixing in 1: 1 is placed in the mixed solvent of ethylene glycol and deionized water (volume ratio is 1: 3) composition Vulcan XC-72 activated carbon powder and SnO
2The addition of nano particle is the 40mg/120ml mixed solvent, and the control temperature is 60 ℃, utilizes powerful stirring of magnetic stirring apparatus fully to mix;
(3) with liquid phase reduction loaded with nano Pd particle:
The PdCl that in the mixed liquor that step (2) obtains, dropwise adds 2mmol/L
2Solution stirred after one hour, and the trisodium citrate that adding contains two crystallizations water is as stabilizing agent; The mol ratio of control metal Pd and trisodium citrate is 1: 5, and ultrasonic concussion 30min mixes; With the pH value to 11 of alkaline solution NaOH regulator solution, add the borane reducing agent sodium hydride then again, continue isothermal reaction 3h; Be cooled to room temperature then, filtering to wash to filter cake does not have Cl
-, vacuum drying 12h promptly obtains the Pd/SnO of black
2/ C catalyst, the load capacity of nanometer Pd particle are 20wt%.
Wherein, Vulcan XC-72 activated carbon powder through preliminary treatment, may further comprise the steps before mixing: the control temperature is 90 ℃, with the HNO of active carbon Vulcan XC-72 at 5mol/L
3In the powerful 5h that stirs, filter and washing after being cooled to room temperature; Control temperature again at 130 ℃ of vacuum drying 6h, grinding the active carbon after handling also, 200 mesh sieve branches obtain even-grained Vulcan XC-72 activated carbon powder.
Embodiment 4
A kind of Pd/SnO
2The preparation method of/C composite nano-catalyst may further comprise the steps:
(1) Hydrothermal Preparation SnO
2Nano particle:
1. take by weighing 0.23g Macrogol 2000 (PEG2000) and be dissolved in the 50ml absolute ethyl alcohol, add 3.2gSnCl again after the dissolving fully
22H
2O forms mixed solution, 50 ℃ of reactions of magnetic agitation temperature control 2h, the 12h of room temperature ageing afterwards;
2. in autoclave, carry out high-temperature high-voltage reaction, filtering drying obtains pale yellow powder and is SnO
2Nano particle.
(2) with Vulcan XC-72 activated carbon powder and SnO
2Nano particle fully mixes in the mixed solution of ethylene glycol and deionized water, and magnetic stirring apparatus is powerful to be stirred;
(3) with liquid phase reduction loaded with nano Pd particle:
1. be active carbon and stannic oxide particle 40mg after taking by weighing processing at 1: 1 according to mass ratio, join in the 120ml water-ethylene glycol solution, (volume ratio of water and ethylene glycol is 1: 3), temperature control evenly stirs for 60 ℃, obtains mixed solution 1;
2. the PdCl that in mixed liquor 1, dropwise adds 2mmol/L
2Solution 46.99ml stirred after one hour, and the trisodium citrate 138.18mg that adding contains two crystallizations water is as stabilizing agent; (mol ratio that is metal Pd and trisodium citrate is 1: 5); Ultrasonic concussion 30min mixes, afterwards with the pH value to 11 of alkaline solution NaOH regulator solution; Add borane reducing agent sodium hydride 21.3mg then, continue isothermal reaction 3h, obtain mixed solution 2;
3. with mixed solution 2 cool to room temperature, filtering to wash to filter cake does not have Cl
-, vacuum drying 12h afterwards; Obtain the Pd-SnO of black
2/ C catalyst, the load capacity of nanometer Pd particle are 20wt%.
(4) after nanometer Pd particulate load is accomplished,, promptly obtain Pd/SnO through suction filtration, oven dry
2/ C composite nano-catalyst.
Wherein, Vulcan XC-72 activated carbon powder before mixing through preliminary treatment: weighing 1g active carbon VulcanXC-72 is at 90 °, (100ml) HNO of 5mol/L
3The powerful 5h that stirs in the solution; Cooling is a room temperature, filters washing; 130 ° of vacuum drying 6h obtain even-grained activated carbon granule with active carbon grinding and 200 mesh sieve branches after handling afterwards.
Claims (6)
1. Pd/SnO
2The preparation method of/C composite nano-catalyst is characterized in that, this method may further comprise the steps:
(1) Hydrothermal Preparation SnO
2Nano particle:
A, Macrogol 2000 (PEG2000) is dissolved in the absolute ethyl alcohol, adds SnCl again after the dissolving fully
22H
2O forms mixed solution, 50 ℃ of temperature controls reaction 2h under the magnetic agitation, ageing 12h at room temperature then;
B, in autoclave, carry out high-temperature high-voltage reaction, filtering drying obtains pale yellow powder and is SnO
2Nano particle;
(2) with Vulcan XC-72 activated carbon powder and SnO
2The nano particle mass ratio is that mixing in 1: 1 is placed in the mixed solvent of ethylene glycol and deionized water composition Vulcan XC-72 activated carbon powder and SnO
2The addition of nano particle is the 40mg/120ml mixed solvent, and the control temperature is 60 ℃, utilizes powerful stirring of magnetic stirring apparatus fully to mix;
(3) with liquid phase reduction loaded with nano Pd particle:
The PdCl that in the mixed liquor that step (2) obtains, dropwise adds 2mmol/L
2Solution stirred after one hour, and the trisodium citrate that adding contains two crystallizations water is as stabilizing agent; The mol ratio of control metal Pd and trisodium citrate is 1: 5, and ultrasonic concussion 30min mixes; With the pH value to 11 of alkaline solution NaOH regulator solution, add reducing agent then again, continue isothermal reaction 3h; Be cooled to room temperature then, filtering to wash to filter cake does not have Cl-, and vacuum drying 12h promptly obtains the Pd/SnO of black
2/ C catalyst.
2. a kind of Pd/SnO according to claim 1
2The preparation method of/C composite nano-catalyst is characterized in that, in the mixed solution described in the step (1), the concentration of Macrogol 2000 is 0.004-0.005g/ml, SnCl
2Concentration be 0.04-0.05g/ml.
3. a kind of Pd/SnO according to claim 1
2The preparation method of/C composite nano-catalyst is characterized in that, the Vulcan XC-72 activated carbon powder described in the step (2) through preliminary treatment, may further comprise the steps before mixing: the control temperature is 90 ℃, with the HNO of active carbon Vulcan XC-72 at 5mol/L
3In the powerful 5h that stirs, filter and washing after being cooled to room temperature; Control temperature again at 130 ℃ of vacuum drying 6h, grinding the active carbon after handling also, 200 mesh sieve branches obtain even-grained Vulcan XC-72 activated carbon powder.
4. a kind of Pd/SnO according to claim 1
2The preparation method of/C composite nano-catalyst is characterized in that, the volume ratio of ethylene glycol described in the step (2) and deionized water is 1: 3.
5. a kind of Pd/SnO according to claim 1
2The preparation method of/C composite nano-catalyst is characterized in that, the reducing agent described in the step (3) is a sodium borohydride.
6. a kind of Pd/SnO according to claim 1
2The preparation method of/C composite nano-catalyst is characterized in that, the Pd/SnO described in the step (3)
2The load capacity of nanometer Pd particle is 20wt% in the/C catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210289402.9A CN102806079B (en) | 2012-08-14 | 2012-08-14 | Preparation method of Pd/SnO2/C composite nanometer catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210289402.9A CN102806079B (en) | 2012-08-14 | 2012-08-14 | Preparation method of Pd/SnO2/C composite nanometer catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102806079A true CN102806079A (en) | 2012-12-05 |
CN102806079B CN102806079B (en) | 2014-12-17 |
Family
ID=47230053
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210289402.9A Expired - Fee Related CN102806079B (en) | 2012-08-14 | 2012-08-14 | Preparation method of Pd/SnO2/C composite nanometer catalyst |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102806079B (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105606656A (en) * | 2015-11-06 | 2016-05-25 | 上海戴维蓝普传感技术有限公司 | Anti-silicon poisoning anti-sulfur-poisoning hot wire methane sensor |
CN106981672A (en) * | 2017-05-12 | 2017-07-25 | 湖北大学 | A kind of fuel battery anode catalysis material and its preparation method and application |
CN108311145A (en) * | 2017-01-17 | 2018-07-24 | 中国科学院上海高等研究院 | The preparation of palladium on carbon tin nanometer alloy catalyst and its application in carbon dioxide electro-catalysis reduction |
CN109110803A (en) * | 2018-08-03 | 2019-01-01 | 中国工程物理研究院化工材料研究所 | More chemical state PdOxModify SnO2Nano composite air-sensitive material and preparation method thereof |
CN110137486A (en) * | 2019-05-21 | 2019-08-16 | 南京工业大学 | A kind of preparation method of the transition metal oxide nano-material synthesized from top to bottom |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1804149A (en) * | 2005-12-01 | 2006-07-19 | 华中师范大学 | SnO2 monodisperse nano monocrystal with square structure and synthesis method thereof |
CN101279255A (en) * | 2008-04-17 | 2008-10-08 | 中国科学院上海微系统与信息技术研究所 | Method for directly preparing nano-catalyst based on Pd for alcohol fuel battery |
-
2012
- 2012-08-14 CN CN201210289402.9A patent/CN102806079B/en not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1804149A (en) * | 2005-12-01 | 2006-07-19 | 华中师范大学 | SnO2 monodisperse nano monocrystal with square structure and synthesis method thereof |
CN101279255A (en) * | 2008-04-17 | 2008-10-08 | 中国科学院上海微系统与信息技术研究所 | Method for directly preparing nano-catalyst based on Pd for alcohol fuel battery |
Non-Patent Citations (1)
Title |
---|
R. MNALEWANE MODIBEDI, ET AL.: "Carbon supported Pd-Sn and Pd-Ru-Sn nanocatalysts for ethanol electro-oxidation in alkaline medium", 《INTERNATIONAL JOURNAL OF HYDROGEN ENERGY》 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105606656A (en) * | 2015-11-06 | 2016-05-25 | 上海戴维蓝普传感技术有限公司 | Anti-silicon poisoning anti-sulfur-poisoning hot wire methane sensor |
CN105606656B (en) * | 2015-11-06 | 2020-04-21 | 上海戴维蓝普传感技术有限公司 | Hot wire type methane sensor with silicon resistance and sulfur poisoning resistance |
CN108311145A (en) * | 2017-01-17 | 2018-07-24 | 中国科学院上海高等研究院 | The preparation of palladium on carbon tin nanometer alloy catalyst and its application in carbon dioxide electro-catalysis reduction |
CN106981672A (en) * | 2017-05-12 | 2017-07-25 | 湖北大学 | A kind of fuel battery anode catalysis material and its preparation method and application |
CN106981672B (en) * | 2017-05-12 | 2019-07-16 | 湖北大学 | A kind of fuel battery anode catalysis material and its preparation method and application |
CN109110803A (en) * | 2018-08-03 | 2019-01-01 | 中国工程物理研究院化工材料研究所 | More chemical state PdOxModify SnO2Nano composite air-sensitive material and preparation method thereof |
CN110137486A (en) * | 2019-05-21 | 2019-08-16 | 南京工业大学 | A kind of preparation method of the transition metal oxide nano-material synthesized from top to bottom |
Also Published As
Publication number | Publication date |
---|---|
CN102806079B (en) | 2014-12-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
Forslund et al. | Enhanced electrocatalytic activities by substitutional tuning of nickel-based ruddlesden–popper catalysts for the oxidation of urea and small alcohols | |
CN104681823B (en) | A kind of nitrogen-doped graphene and Co3O4 hollow nano-sphere composites and its preparation method and application | |
CN105170169B (en) | A kind of nitrogen-doped graphene iron-based nano-particles reinforcement type catalyst and preparation method thereof | |
CN108963282A (en) | A kind of fuel cell carbon carried platinum-based catalyst and the preparation method and application thereof of solvent-thermal method reduction | |
CN106025301B (en) | A kind of preparation and application of carried metal organic frame compound nitrogen functional carbon material | |
CN101944620B (en) | Fuel cell catalyst taking multi-element compound as carrier and preparation method thereof | |
CN111001428B (en) | Metal-free carbon-based electrocatalyst, preparation method and application | |
CN109718822B (en) | Method for preparing metal-carbon composite catalytic material and application thereof | |
CN107335451B (en) | Platinum/molybdenum disulfide nano sheet/graphene three-dimensional combination electrode catalyst preparation method | |
CN101814607A (en) | Preparation method of platinum/graphen catalyst for proton exchange membrane fuel cell | |
CN105529472A (en) | Co-N double-doped flaky porous two-dimensional carbon material and preparation method thereof | |
CN102806079B (en) | Preparation method of Pd/SnO2/C composite nanometer catalyst | |
CN103143378A (en) | Preparation method of non-noble metal oxygen reduction electrocatalyst for cathode of fuel cell | |
CN105289687A (en) | Nitrogen-doped graphene-supported iron-based nanoparticle composite catalyst and preparation method thereof | |
CN106757143A (en) | A kind of water decomposition reaction catalysis electrode and preparation method thereof | |
CN109524679B (en) | High-efficiency electrocatalytic methanol oxidation fuel cell catalyst and preparation method thereof | |
CN104437475A (en) | Electro-catalyst Pt/amTiO2/rGO and preparation method | |
CN102867965A (en) | Porous microsphere perovskite type calcium manganese oxide compound and preparation method and application thereof | |
Yu et al. | Facile route to achieve bifunctional electrocatalysts for oxygen reduction and evolution reactions derived from CeO 2 encapsulated by the zeolitic imidazolate framework-67 | |
CN111634954A (en) | Iron-modified cobalt-iron oxide with self-assembled flower ball structure and preparation and application thereof | |
CN104707625A (en) | Preparation method of Pt-Ag-Co/C catalyst | |
CN103022520A (en) | Fuel-cell catalyst Pt/WO3 and application thereof | |
CN111430737A (en) | Copper-platinum alloy nanoparticle loaded nitrogen-doped three-dimensional porous carbon material and preparation method and application thereof | |
CN101814608A (en) | Anode composite catalyst Pt-MoOx for direct methanol fuel cells, and preparation method thereof | |
CN103191757A (en) | PdNiW/C ternary alloy nano catalyst and preparation method thereof |
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 | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141217 Termination date: 20170814 |