Method for preparing supported metal catalyst with high dispersion active center

A metal catalyst and supported technology, which is applied in the field of preparation of supported metal catalysts, can solve the problems of high catalyst production cost, unfavorable large-scale application, low reaction temperature, etc., and achieve simple and reliable preparation process, increased dispersion, The effect of using less

Active Publication Date: 2013-05-01
GUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The prepared catalyst has high uniformity, the reaction process is simple and easy to control, the catalyst has high dispersion, high specific surface area and good pore size, the reaction temperature is low during the preparation process, and the crystal form and particle size of nanoparticles are controllable; however, it is widely used in practical applications Metal-organic compound or organic gelling agent, catalyst production cost is higher (Angewandte Chemie Volume35(1996), 1420-1436 and Catalysis Today Volume137(2008), 132-143); Philippe Serp et al. (Chemical Reviews Volume102(2002), 3085 -3128) reviewed the preparation of supported catalysts by chemical vapor deposition (i.e., gas phase impregnation-decomposition method). The metal active precursor was vaporized and then deposited on the carrier, and finally heated and roasted to decompose. Compared with the conventional impregnation method, the metal active component The distribution is more uniform and the activity is much improved, but the metal prerequisite requires easy vaporization and decomposition
The metal precursors commonly used in the actual process are metal carbonyl compounds. Due to their high toxicity, anhydrous and oxygen-free preparation conditions are required, which is not conducive to large-scale application.

Method used

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  • Method for preparing supported metal catalyst with high dispersion active center
  • Method for preparing supported metal catalyst with high dispersion active center
  • Method for preparing supported metal catalyst with high dispersion active center

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Example 1: Effect of Metal Loading

[0026] Weigh 2.5g granular 40-60 mesh commercial carrier SiO 2 Dry at 120°C for 12 hours and set aside. At room temperature, add ethylene glycol (glycol, abbreviated as EG) to impregnate SiO 2 The carrier was dried for 6 hours, and then dried at 50° C. for 24 hours to obtain a surface-modified carrier. At room temperature, 2.4692g Co(NO 3 ) 2 ·6H 2 O aqueous solution, soaked for 12 hours, 90°C spin-dried for 12 hours, 120°C dried for 12 hours, dried samples were placed in a muffle furnace at 400°C for 2 hours, the heating rate was 2°C / min, and 10% loaded Co / SiO 2 Catalyst, changing Co(NO 3 ) 2 ·6H 2 The amount of O, repeat the above process, the resulting catalyst is recorded as 1%Co-SiO 2 , 10%Co-SiO 2 , 20%Co-SiO 2 , 25%Co-SiO 2 , 30%Co-SiO 2 , 40%Co-SiO 2 . For the corresponding XRD spectrum, see figure 1 , it can be concluded from the figure that when the metal loading is below 25wt%, the metal active center is ...

Embodiment 2

[0027] Embodiment 2: the influence of sintering temperature

[0028] Implementation steps and conditions are the same as embodiment 1, commercial carrier SiO 2 Dry at 100°C for 24 hours with 10% Co / SiO loading 2 Catalyst as an example. At room temperature, add ethylene glycol (EG) to impregnate SiO 2 The carrier was dried for 24 hours, and then dried at 150° C. for 6 hours to obtain a surface-modified carrier. Co(NO 3 ) 2 ·6H 2 Immerse after O for 20 hours, spin dry at 50°C for 24 hours, and dry at 200°C for 10 hours. After drying, the sample is placed in a muffle furnace and roasted for 2 hours at 300°C, 400°C, 500°C, 600°C, 700°C, and 800°C. Rate 2°C / min. For the corresponding XRD spectrum, see figure 2 , the active center of the sample whose calcination temperature is below 600℃ is on the carrier SiO 2The loading is very uniform, the dispersion is very high, and the XRD diffraction peak completely disappears; at a calcination temperature above 600°C, a very diffus...

Embodiment 3

[0029] Embodiment 3: the influence of ethylene glycol dosage

[0030] Weigh 2.5g granular 40-60 mesh commercial carrier SiO 2 Dry at 200°C for 6 hours and set aside. At room temperature, 2.4692g Co(NO 3 ) 2 ·6H 2 O in ethylene glycol aqueous solution, soaked for 6 hours, spin-dried at 60°C for 20h, and dried at 100°C for 24 hours; after drying, the sample was placed in a muffle furnace and calcined at 400°C for 2 hours at a heating rate of 2°C / min to obtain 10 % load Co / SiO 2 Catalyst; wherein the molar ratios of the metal in the metal salt to ethylene glycol are: 1:0.5, 1:1, 1:2, 1:4, 1:6, 1:10. For the corresponding XRD spectrum, see image 3 , it can be concluded from the figure that when the molar ratio of metal to ethylene glycol in the metal salt solution is less than 1:1, the metal active center is on the carrier SiO 2 The load is very uniform, the dispersion is very high, and the XRD diffraction peak completely disappears; when the ratio is 1:1, a very diffuse X...

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Abstract

The invention discloses a method for preparing a supported metal catalyst with a high dispersion active center. An improved impregnation method is adopted, i.e. a catalyst conventional carrier is impregnated in a polyfunctional compound comprising more than two hydroxy-philic functional groups after being subjected to drying preprocessing and then is impregnated in aqueous solution of metal salt after being dried; or, a carrier which is not subjected to surface modification is directly impregnated in aqueous solution of metal salt of the polyfunctional compound comprising more than two hydroxy-philic functional groups; and then the metal supported catalyst by drying and calcination. By the improved impregnation method, i.e. a complexation impregnation method, effects of the carrier and the active center can be improved; the use amount of the polyfunctional compound is small and is easy to control; the preparation technical process is simple and reliable; the method disclosed by the invention is a novel approach for preparing a high-efficiency catalyst; and according to the catalyst prepared by the complexation impregnation method, metal active components are uniformly distributed on the surface of the catalyst, the dispersity is improved, the particle size of the active components can be controlled in the range of 10nm, and the particle size distribution is adjustable.

Description

Technical field: [0001] The invention belongs to the technical field of catalysts, and in particular relates to a preparation method of a loaded metal catalyst with highly dispersed active centers. Background technique: [0002] Supported catalysts are commonly used catalysts in the chemical industry, and the metal active components can be uniformly dispersed on the surface of the catalyst. Supported catalysts generally use less metal, and the preparation process is simple and easy to control. Common methods for preparing supported catalysts include impregnation, ion exchange, sol-gel and co-precipitation. In order to prepare catalysts with higher dispersion and higher activity, new preparation methods are constantly emerging. For example: use cold / hot plasma to prepare ultra-fine particle catalysts, and plasma sputtering to assist the deposition of catalyst active components to prepare highly dispersed and highly active catalysts. However, special plasma devices are requi...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J37/02B01J23/75B01J23/72B01J23/755B01J29/76
Inventor 王铁军仇松柏马隆龙张琦刘琪英张雪
Owner GUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI
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