Sintering-resisting loading type nanometer palladium catalyst and preparing method and application thereof

A supported catalyst technology, which is applied in the field of anti-sintering nano-Pd catalysts, can solve the problems of industrial application limitations, long preparation cycle, cumbersome preparation process, etc., and achieve improved anti-sintering performance, excellent CO ignition performance, and improved dispersion. Effect

Inactive Publication Date: 2013-01-16
XIAMEN UNIV
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Although the catalyst prepared by this method can effectively inhibit the agglomeration of metal particles in a certain temperature range, its high temperature (>700°C) stability) still needs to be improved, and due to the special structure of the encapsulated catalyst, the reactants must first Diffusion passes through the cladding layer to reach the metal active center, and there is a contact problem between the metal active phase and the sub

Method used

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  • Sintering-resisting loading type nanometer palladium catalyst and preparing method and application thereof
  • Sintering-resisting loading type nanometer palladium catalyst and preparing method and application thereof
  • Sintering-resisting loading type nanometer palladium catalyst and preparing method and application thereof

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[0025] Example 1

[0026] Weigh 10g SiO 2 The carrier (Aldrich Chemical Company, 35~60 mesh), soaked in 20% dilute nitric acid solution for 24h, stirred 3~5 times during the period, then washed with distilled water to pH=7.0, dried at 110°C for 12h, and set aside. 2g of processed SiO 2 Soaked in 6ml Pd with a mass concentration of 1.04mg / ml for 24h, then dried at 110°C for 12h, roasted in air at 800°C for 2h, heating rate 10°C / min, and 600°C in high purity hydrogen C reduction for 0.5h to obtain 3wt%Pd / SiO 2 -800-Air catalyst, denoted as Cat 1, the particle size of Pd particles is 3.1nm, see figure 1 with 2 .

[0027] Weigh 10 mg of the above catalyst Cat 1 into a micro fixed-bed flow reactor. 2 In the air flow, the temperature is increased to 600°C at a rate of 20°C / min, reduced for 30 minutes, and reduced to room temperature, then use high purity He to purge for about 20 minutes, and then switch to CO / O 2 / He (1 / 1 / 98, volume ratio) reactant gas for heating up reaction, the heatin...

Example Embodiment

[0034] Example 2

[0035] The implementation steps and conditions are the same as in Example 1, except that the catalyst calcination atmosphere is changed from air to N 2 , Get 3wt%Pd / SiO 2 -800-N 2 The catalyst, denoted as Cat 2, the particle size of Pd particles is 3.8nm, see Figure 5 with 6 , Its CO oxidation reaction performance results are shown in Table 1.

Example Embodiment

[0038] Example 3

[0039] The implementation steps and conditions are the same as in Example 1, except that acetylacetone used as the solvent for palladium acetylacetonate is replaced with toluene to obtain 3wt%Pd / SiO 2 -800-Air-2 catalyst, denoted as Cat 3, the particle size of Pd particles is 3.1nm, and its CO oxidation reaction performance results are shown in Table 1.

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Abstract

A sintering-resisting loading type nanometer palladium catalyst and a preparing method and application thereof relate to a nanometer metal catalyst. The sintering-resisting loading type nanometer palladium catalyst contains active component acetylacetone palladium and carrier SiO2, and metal Pd occupies 0.5-5.0% of the sintering-resisting loading type nanometer palladium catalyst according to mass percent. The preparing method of the sintering-resisting loading type nanometer palladium catalyst includes steps: (1) SiO2 is selected to serve as the carrier, immersed into nitric acid solution and washed until the pH of SiO2 is 6.5-7.0, and then is dried; (2) Pd (acac) 2 compound is dissolved in acetylacetone or toluene solvents to prepare Pd (acac) 2 solution with mass concentration of Pd to be 0.26-1.04 mg/ml; (3) SiO2 obtained in the step (1) is immersed into the metal salt solution obtained in the step (2), and an initial catalyst is obtained after drying and roasting; and (4) the initial catalyst obtained in the step (3) is subjected to hydrogen gas reduction, and the sintering-resisting loading type nanometer palladium catalyst is finally obtained.

Description

technical field [0001] The invention relates to a nanometer metal catalyst, in particular to a sintering-resistant nanometer Pd catalyst, which is prepared by a simple impregnation method and its application in CO oxidation reaction. Background technique [0002] Supported Pd catalyst is one of the most important metal catalysts, which can be widely used in reactions such as olefin hydrogenation, alcohol oxidation, coupling reaction, automobile exhaust elimination, CO oxidation treatment, etc. The size is closely related, usually the Pd catalyst with smaller particles has better catalytic performance. Okada et al. (Catalysis Today, 2011, doi:10.1016 / j.cattod.2011.08.014) compared the preparation of nano-Pd / SiO by deposition and impregnation methods 2 It was found that the particle size of Pd on the catalyst prepared by the deposition method (3.9nm) was significantly smaller than that of the catalyst prepared by the impregnation method (6~12nm), and the former was more condu...

Claims

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Application Information

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IPC IPC(8): B01J23/44C01B31/20C01B32/50
Inventor 翁维正李兵章青万惠霖
Owner XIAMEN UNIV
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