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Method for preparing high-dispersion metal catalyst

A metal catalyst, highly dispersed technology, applied in the direction of molecular sieve catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc. Performance, harsh raw material storage conditions and other issues, to achieve excellent stability, simple and convenient preparation method, easy storage effect

Inactive Publication Date: 2019-10-25
DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

These methods all have the following one or more deficiencies: complex preparation process, harsh raw material storage conditions and high preparation costs
The impregnation method has become a widely used method for preparing supported metal nanocatalysts in industry because of its simple preparation method and low price. However, this method is not easy to prepare catalysts with highly dispersed active components, so it usually cannot show very high catalytic activity performance
There are few reports on the preparation of highly dispersed metal catalysts by impregnation, and there are no relevant reports on the preparation of highly dispersed catalysts by impregnation using alcohol amines as modifiers.

Method used

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  • Method for preparing high-dispersion metal catalyst
  • Method for preparing high-dispersion metal catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0025] Select silica pellets produced by Shandong Ocean Chemical Industry Co., Ltd. as the carrier precursor, weigh 5g of the above precursor and place it in a beaker, add 15g of ethanolamine, soak for 6h, and dry the mixture at 90°C for 96h in an air atmosphere. Calcined for 24 hours under air atmosphere to obtain the carrier required for catalyst preparation.

[0026] 2.83g Cu(NO 3 ) 2 ·3H 2 O was dissolved in 5ml of deionized water, 3g of the above-mentioned carrier obtained by ethanolamine treatment was added into the solution, soaked at room temperature for 12h, dried at 50°C for 48h, and then calcined at 350°C for 3h to obtain the catalyst, denoted as A. The XRD figure of gained catalyst is as follows figure 1 shown.

[0027] The composition of the catalyst A is as follows in terms of mass fraction: 20% of Cu, and 80% of the carrier obtained by ethanolamine treatment.

Embodiment 2

[0029] Select silicon oxide produced by Shandong Ocean Chemical as the carrier precursor, weigh 5g of the above precursor and place it in a beaker, add 50g of triethanolamine, soak for 12h, and dry the mixture at 150°C for 48h in air atmosphere, and the obtained solid is heated at 350°C in air Calcined under the atmosphere for 10 hours to obtain the carrier required for catalyst preparation.

[0030] 2.61g Co(NO 3 ) 2 ·6H 2 O was dissolved in 10ml of deionized water, 3g of the carrier obtained by the above-mentioned triethanolamine treatment was added into the solution, soaked at room temperature for 12h, dried at 120°C for 12h, and then calcined at 250°C for 4h to obtain the catalyst, denoted as B. The XRD figure of gained catalyst is as follows figure 1 shown.

[0031] The composition of catalyst B is as follows in terms of mass fraction: Co is 15%, and the support obtained by triethanolamine treatment is 85%.

Embodiment 3

[0033] Select silicon oxide powder produced by Shandong Ocean Chemical as the carrier precursor, weigh 5g of the above precursor and place it in a beaker, add 5g of n-propanolamine, soak for 6h, and dry the mixture at 50°C for 120h in an air atmosphere. Calcined at 550° C. for 1 h in an air atmosphere to obtain the carrier required for catalyst preparation.

[0034] 5.24g Ni(NO 3 ) 2 ·6H 2 O was dissolved in 15ml of deionized water, 3g of the carrier obtained by the above-mentioned n-propanolamine treatment was added to the solution, soaked at room temperature for 12h, dried at 150°C for 6h, and then calcined at 550°C for 1h to obtain the catalyst, which was designated as C. The XRD figure of gained catalyst is as follows figure 1 shown.

[0035] The composition of catalyst C is as follows in terms of mass fraction: Ni is 30%, and the support obtained by n-propanolamine treatment is 70%.

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Abstract

The invention provides a method for preparing a high-dispersion metal catalyst, and belongs to the technical field of catalyst preparation methods. The method includes the steps that an oxide carrieris pretreated by alcohol amine, and then the carrier is loaded with metal in a high dispersion mode through an impregnation method. The method for preparing the catalyst is simple and convenient, therequirements for equipment are low, the method is friendly to the environment, and large-scale production is easy. The catalyst prepared through the method has high metal dispersion, and the activityand stability of the catalyst can be improved. Specially, a copper-silicon catalyst prepared through the method is suitable for being used as a catalyst for preparing furfuryl alcohol or methyl furanthrough furfural selective hydrogenation.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation methods, and in particular relates to a method for preparing highly dispersed metal catalysts. Background technique [0002] The metal dispersion of the supported catalyst has an important influence on the reactivity of the catalyst. Generally speaking, in order to improve the reactivity of catalysts and reduce the amount of metals used, increasing the metal dispersion is an effective way. There are many related reports on improving metal dispersion. [0003] Patent CN 10587987 A discloses a method for preparing a highly dispersed nickel-based catalyst. The invention adopts a precipitation method to deposit nickel onto a modified diatomite carrier. Patent CN 102553592 A discloses the preparation of SiO by ion exchange method 2 The method for supporting a highly dispersed copper catalyst has a simple preparation process, but the method is suitable for preparing a catalyst with a cop...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J35/00B01J23/72B01J37/02C07D307/44B01J37/08B01J23/75B01J23/755
CPCB01J37/0207B01J23/72C07D307/44B01J37/0018B01J23/75B01J23/755B01J2229/18B01J35/394
Inventor 张宗超杜虹
Owner DALIAN INST OF CHEM PHYSICS CHINESE ACAD OF SCI
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