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Single-atom noble metal catalysts prepared by ultrasonic-assisted displacement reaction and method thereof

A noble metal catalyst and replacement reaction technology, applied in chemical instruments and methods, physical/chemical process catalysts, chemical/physical processes, etc., can solve problems such as high cost, poor activity, unstable catalyst, etc., and achieve easy operation and good conditions Gentle, powerful effect

Active Publication Date: 2020-08-18
SOUTH CHINA UNIV OF TECH
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  • Abstract
  • Description
  • Claims
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Problems solved by technology

The mass-selected soft landing method (Vajda S, White M G. Catalysis applications of size-selected cluster deposition[J]. ACSCatalysis, 2015, 5(12): 7152-7176) is a physical deposition method with mild reaction conditions, but Its cost is too high and the yield is very low, and it is not suitable for supports with high specific surface area and mesoporous; wet chemical method (Guo X, Fang G, Li G, et al. Direct, nonoxidative conversion of methane to ethylene, aromatics , and hydrogen[J]. Science, 2014, 344(6184): 616-619) including impregnation method, co-precipitation method, precipitation-deposition method and strong electrostatic adsorption method. The components do not contact the substrate and the activity is poor, the catalyst prepared by the strong electrostatic adsorption method is not stable, and the metal loading is relatively low; the atomic layer deposition method (Sun S, Zhang G, Gauquelin N, et al. Single-atom catalyst using Pt / graphene achieved through atomic layer deposition[J]. Scientific Reports,2013, 3, 1775-1784) is a method with certain general applicability for the preparation of single-atom catalysts, but it has specific requirements for instruments and requires the use of boiling point Lower organic metals are used as metal precursors, and the cost is higher; organometallic complex method (Serna P, Gates B C. Molecular metal catalysts on supports: organometallic chemistry meets surface science[J]. Accounts of Chemical Research, 2014, 47( 8): 2612-2620) require that the ligand or metal center must be able to form a strong bond with the functional group of the carrier, and it is only suitable for theoretical research and not for industrial applications; MOFs precursor roasting method (Yin P, Yao T, Wu Y, et al.Single Cobalt Atoms with Precise N-Coordination as Superior Oxygen ReductionReaction Catalysts[J]. ndte Chemie International Edition, 2016, 55(36):10800-10805) is simple to prepare, but limited to the preparation of non-noble metal single-atom catalysts
In addition, photochemical reduction (LiuP, Zhao Y, Qin R, et al. Photochemical route for synthesizing atomically dispersed palladium catalysts[J]. Science, 2016, 352(6287): 797-800) and carbon-based material pyrolysis have also been reported. It is used to prepare single-atom catalysts, but it has higher requirements on the reaction operating environment and carrier
Considering the advantages and disadvantages of the above-mentioned preparation methods of single-atom catalysts, it is still a great challenge to develop a preparation method of single-atom noble metal catalysts with simple operation, low cost and certain universality.

Method used

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  • Single-atom noble metal catalysts prepared by ultrasonic-assisted displacement reaction and method thereof
  • Single-atom noble metal catalysts prepared by ultrasonic-assisted displacement reaction and method thereof
  • Single-atom noble metal catalysts prepared by ultrasonic-assisted displacement reaction and method thereof

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Effect test

Embodiment 1

[0044] Zn(NO 3 ) 2 ·6H 2 O and Co(NO 3 ) 2 ·6H 2 O was dissolved in 50 ml of anhydrous methanol at a molar ratio of 97:3 (4.4 mmol in total) as solution A; 1.46 g of dimethylimidazole was weighed and dissolved in 50 ml of anhydrous methanol as solution B. Then ultrasonically disperse evenly, and in the state of stirring, add liquid B to liquid A drop by drop, and continue to stir for 12 h. Centrifuge and wash with anhydrous methanol. The sample obtained by centrifugation was dried at 60 °C, ground and dried in vacuum to obtain Zn with clean pores. 97 co 3 -ZIF.

[0045] The prepared Zn 97 co 3 - ZIF is evenly spread in the quartz porcelain boat, put into the tube furnace and calcined under high-purity Ar (flow rate 40ml / min). The calcination procedure was as follows: first, keep at 30 °C for 60 min, then raise the temperature to 950 °C at 2 °C / min, keep for 2 h, and finally lower the temperature to room temperature at a cooling rate of 5 °C / min. The obtained Co SAs...

Embodiment 2

[0049] Zn(NO 3 ) 2 ·6H 2 O and Co(NO 3 ) 2 ·6H 2 O was dissolved in 50 ml of anhydrous methanol at a molar ratio of 98:2 (4.4 mmol in total) as solution A; 2.92 g of dimethylimidazole was weighed and dissolved in 50 ml of anhydrous methanol as solution B. Then ultrasonically disperse evenly, and in the state of stirring, add liquid B to liquid A drop by drop, and continue to stir for 6 h. Centrifuge and wash with anhydrous methanol. The sample obtained by centrifugation was dried at 60 °C, ground and dried in vacuum, and Zn with clean pores could be obtained. 98 co 2 -ZIF.

[0050] The prepared Zn 98 co 2 - ZIF is evenly spread in the quartz porcelain boat, put into the tube furnace in high-purity N 2 (flow rate 40ml / min) for calcination. The calcination procedure is as follows: first, keep at 30 °C for 60 min, then raise the temperature to 1000 °C at 2 °C / min, keep for 2 h, and finally cool down to room temperature at a cooling rate of 10 °C / min. The obtained Co...

Embodiment 3

[0054] Zn(NO 3 ) 2 ·6H 2 O and Co(NO 3 ) 2 ·6H 2 O was dissolved in 50 ml of anhydrous methanol at a molar ratio of 98:2 (4.4 mmol in total) as solution A; 2.92 g of dimethylimidazole was weighed and dissolved in 50 ml of anhydrous methanol as solution B. Then ultrasonically disperse evenly, and in the state of stirring, add liquid B to liquid A drop by drop, and continue to stir for 24 h. Centrifuge and wash with anhydrous methanol. The sample obtained by centrifugation was dried at 60 °C, ground and dried in vacuum, and Zn with clean pores could be obtained. 98 co 2 -ZIF.

[0055] The prepared Zn 98 co 2 - ZIF is evenly spread in the quartz porcelain boat, put into the tube furnace and calcined under high-purity Ar (flow rate 40ml / min). The calcination procedure was as follows: first, keep at 30 °C for 60 min, then raise the temperature to 1000 °C at 2 °C / min, keep for 2.5 h, and finally cool down to room temperature at a cooling rate of 5 °C / min. The obtained Co...

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Abstract

The invention discloses a monatomic noble metal catalyst prepared by ultrasonic assisted replacement reaction and a method thereof. The method mainly includes the steps of: synthesizing metal ratio adjustable ZnxMy-ZIF (M can be Co, Cu, Ni and other metals, and ZIF is zeolite imidazate framework structural material) at room temperature, and then performing high-temperature calcinations in an inertatmosphere to obtain M SAs-CN-y (y represents the molar percentage of M), and finally adding M SAs-CN-y into water in an inert atmosphere, adding a noble metal salt solution under an ultrasonic condition for reaction, thus obtaining a monatomic state dispersed noble metal catalyst. The method has a wide option range of noble metal salt, is suitable for preparation of Pt SAs-CN, Pd SAs-CN, Ru SAs-CN and other noble metal monatomic catalysts, has universality, also the preparation method is simple, and the obtained catalyst has highly dispersed noble metal atoms, which are distributed in an N doped carbon carrier in a monatomic distribution state.

Description

technical field [0001] The invention relates to the technical field of single-atom catalysts and their preparation, in particular to single-atom noble metal catalysts prepared by ultrasonic-assisted displacement reactions and methods thereof. Background technique [0002] In recent years, single-atom catalysts have attracted increasing research interest in the fields of materials and catalysis due to their ultrahigh catalytic activity and efficient chemoselectivity. The active metal components in single-atom catalysts are highly dispersed and present a state of single-atom distribution. Compared with the disadvantages of traditional large-particle metal nanocatalysts that only surface atoms can be used as catalytic active sites, but internal atoms cannot be used, almost 100% of the active component atoms in single-atom catalysts can be used as active sites, thus greatly improving It improves its catalytic activity and can greatly reduce the amount of metal used, which is es...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/24
CPCB01J27/24
Inventor 李映伟邹欣伟沈葵
Owner SOUTH CHINA UNIV OF TECH