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Method for producing carbon-supported Pt shell-core catalyst by means of liquid phase reduction of H2

A catalyst and reducing agent technology, applied in the field of preparation of high-performance low-Pt shell-core catalysts, can solve the problems of insufficient activity, stability, loading, and cost, and achieve high-efficiency oxygen reduction activity, good activity and stability, and catalysts. low load effect

Active Publication Date: 2020-02-04
TSINGHUA UNIV +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] At present, the commonly used commercial catalyst in proton exchange membrane fuel cells is Pt / C, which is a supported catalyst prepared by dispersing Pt nanoparticles on a carrier such as carbon powder XC-72. There are certain deficiencies in stability, capacity, cost, etc.

Method used

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  • Method for producing carbon-supported Pt shell-core catalyst by means of liquid phase reduction of H2
  • Method for producing carbon-supported Pt shell-core catalyst by means of liquid phase reduction of H2
  • Method for producing carbon-supported Pt shell-core catalyst by means of liquid phase reduction of H2

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0045] Take PVP (polyvinylpyrrolidone) 0.057g and dissolve it in a mixed solution of 50mL ethanol and 30mL water, add 0.1M CuCl 2 Solution 2mL, add carbon carrier XC-72 50mg, ultrasonic dispersion 30min. in N 2 Under protection, in an oil bath at 80°C, add 0.03g of alkaline reducing agent NaBH4, including 0.015g of NaOH, 30mL of water, N 2 Protected at 80°C and stirred for 1h. Add 0.015mol / L H 2 PtCl 6 Solution 3mL,N 2 Under protection, replace for 2h. Added oxalate chelated MoCl 5 (0.02g) and H 2 PtCl 6 (0.015mol / L, 3mL) mixed solution, adjust pH=11, in H 2 Under reducing conditions, react at 80°C for 4h to prepare the alloy shell structure. Add NaBH 4 0.2g, NaOH0.06g, in N 2 The crystals were aged overnight under protection. Centrifuge and dry at 60°C to obtain a highly active low-platinum Pt alloy core-shell catalyst.

Embodiment 2

[0047] Take PVP (polyvinylpyrrolidone) 0.057g and dissolve it in a mixed solution of 50mL ethanol and 30mL water, add 0.1M CuCl 2 Solution 2mL, add carbon carrier XC-72 50mg, ultrasonic dispersion 30min. in N 2 Under protection, 80°C oil bath, add alkaline reducing agent NaBH 4 0.03g, of which NaOH 0.015g, water 30mL, N 2 Protected at 80°C and stirred for 1h. Add 0.015mol / L H 2 PtCl 6 Solution 3mL,N 2 Under protection, replace for 2h. Added oxalate chelated MoCl 5 (0.02g) and H 2 PtCl 6(0.015mol / L, 3mL) mixed solution, adjust pH=5, in H 2 Under reducing conditions, react at 80°C for 4h to prepare the alloy shell structure. Add NaBH 4 0.2g, NaOH 0.06g, in N 2 The crystals were aged overnight under protection. Centrifuge and dry at 60°C to obtain a highly active low-platinum Pt alloy core-shell catalyst.

Embodiment 3

[0049] Electrochemical tests were performed in a three-electrode system to characterize the oxygen reduction activity of the catalysts. The electrolyte solution of this system is 0.1mol L -1 HClO 4 , the counter electrode is a Pt sheet electrode, the reference electrode is a saturated calomel electrode, and the cyclic voltammetry test electrolyte solution is N 2 Saturation, the test system is Gamry3000; ORR test solution is O 2 saturation. Preparation of the catalytic layer of the rotating disk electrode membrane: 40% Pt / C catalyst: 5mg catalyst, 2.5mL isopropanol, ultrasonication; add 50 μL of 5wt% Nafion solution, ultrasonication, take 3.2 μL of the above dispersed slurry and coat it on a rotating disk electrode The disc electrode surface, as the working electrode. Due to the low loading of Cu@PtMo / C catalyst, preparation of membrane catalyst layer: 5mg catalyst, 2.5mL isopropanol, ultrasonication; add 50μL of 5wt% Nafion solution, ultrasonication, take 8μL of the above ...

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Abstract

The invention relates to a method for producing a low-platinum alloy shell-core structure catalyst by means of liquid phase system reduction of H2, in particular to a nano-alloy catalyst with a non-noble metal core coated by a Pt alloy shell. The method for producing the low-platinum alloy shell-core structure catalyst by means of liquid phase system reduction of H2 comprises the following steps:(1) dispersing and loading a non-noble metal precursor; (2) reducing and supporting a non-noble metal core; (3) conducting replacement and coating by means of a transition noble metal shell; (4) underthe reducing action of H2, reducing a noble metal alloy shell, and conducting coating by means of the noble metal alloy shell; (5) conducting crystal ageing and growing; and (6) conducting centrifugation and drying to obtain the low-platinum shell-core alloy catalyst. The obtained nanometer core-shell alloy catalyst with the non-noble metal core coated by Pt and the Pt alloy shell is in a form ofultrafine nanoparticles, has efficient oxygen reduction activity, is low in catalyst loading capacity and good in activity and stability, and has important application values in the fields of fuel cells and electrochemical oxygen reduction catalysis processes.

Description

technical field [0001] The invention belongs to the technical field of fuel cells and electrochemical catalysis, and in particular relates to a preparation method of a high-performance low-Pt core-shell catalyst. The catalyst has excellent oxygen reduction activity and is of great value in hydrogen fuel cells and oxygen reduction catalysis processes and apply. Background technique [0002] As an efficient energy conversion device that converts chemical energy into electrical energy, proton exchange membrane fuel cells have important applications in the fields of power transportation, fixed power stations, portable power supplies, cogeneration of heat and power, etc. The advantages of fast start-up, clean, environmentally friendly and noiseless (Zhao Zipeng et al., Advanced materials, 2019). In recent years, breakthroughs have been made in the performance of fuel cells, but there is a large gap between the specific power of domestic fuel cell stacks and the international lev...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/89B01J37/18B82Y30/00B82Y40/00B01J37/16B01J37/03B01J37/34H01M4/88H01M4/92
CPCB01J23/8993B01J37/18B01J37/343B01J37/16B01J37/031B82Y30/00B82Y40/00H01M4/926H01M4/8825B01J35/397B01J35/23B01J35/33Y02E60/50
Inventor 赵卿王诚王海峰王建龙唐亚平
Owner TSINGHUA UNIV