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Cu-ZnO/SiO2 aerogel bimetallic catalyst, as well as preparation method and application thereof

A bimetallic catalyst and airgel technology, applied in the direction of physical/chemical process catalysts, chemical instruments and methods, and the preparation of organic compounds, can solve the problems of single raw materials, high price anhydrous methanol, and low equipment investment, and achieve The effect of simple preparation process, good catalytic activity and stability

Inactive Publication Date: 2017-09-15
JIANGSU UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

In addition, the reaction device provides favorable conditions for the deep processing of high value-added products such as formic acid, ester acid and acetic anhydride; disadvantages: need to use anhydrous methanol with a higher price; must use CO with a concentration higher than 80%; (3) Methanol catalysis Dehydrogenation method, methanol direct dehydrogenation method to prepare methyl formate has the advantages of single raw material, low equipment investment, environmental friendliness and by-production of hydrogen, etc. Southwest Research Institute of Chemical Industry in my country has developed an industrial device with an annual output of 2kt, and the conversion rate of methanol is 30 %-40%, methyl formate selectivity reaches about 80%
In the process of preparing methyl formate by catalytic dehydrogenation of methanol, the conversion rate of methanol and the yield of methyl formate are low. Research and development of new catalysts in order to maximize the single-pass yield of methyl formate is still a research hotspot at present.

Method used

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  • Cu-ZnO/SiO2 aerogel bimetallic catalyst, as well as preparation method and application thereof
  • Cu-ZnO/SiO2 aerogel bimetallic catalyst, as well as preparation method and application thereof
  • Cu-ZnO/SiO2 aerogel bimetallic catalyst, as well as preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0017] Catalyst preparation:

[0018] Cu-ZnO / SiO 2 Airgel (Cu:ZnO:SiO 2 Airgel = 10:2:88, W / W) The catalyst was prepared by co-precipitation method: Weigh 8.8g of SiO 2 Add the airgel into a three-neck flask containing 200ml of deionized water, and stir rapidly in a constant temperature water bath at 65°C to make it evenly dispersed. Prepare 1mol L -1 Na 2 CO 3 For 1L of solution, 3.8009g of Cu(NO 3 ) 2 ·3H 2 O and 0.7311g of Zn(NO 3 ) 2 ·6H 2 O mixed aqueous solution and Na 2 CO 3 The solution was added dropwise into a three-necked flask, stirred vigorously, and adjusted by Na 2 CO 3 The flow velocity of solution makes the pH value of the reaction mixture in the flask stabilize between 7.5 ± 0.2, when Cu(NO 3 ) 2 ·3H 2 O and Zn(NO 3 ) 2 ·6H 2 After the O mixed aqueous solution was added completely, the stirring was continued for 2h. Then filter and wash with deionized water. After washing, the sample was dried overnight at 120° C., calcined at 450° C. for...

Embodiment 2

[0026] Same as Example 1, but changing the loadings of Cu and ZnO in the catalyst so that the loadings of Cu and ZnO are 10% and 3% respectively, the results are shown in Table 2.

[0027] Table 2. Cu(10)-ZnO(3) / SiO 2 Feedstock conversion and reaction product selection for airgel-catalyzed methanol dehydrogenation

[0028]

Embodiment 3

[0030] Same as Example 1, but changing the loading of Cu and ZnO in the catalyst, so that the loading of Cu and ZnO are 20% and 3% respectively, the results are shown in Table 3.

[0031] Table 3. Cu(20)-ZnO(3) / SiO 2 Feedstock conversion and reaction product selection for airgel-catalyzed methanol dehydrogenation

[0032]

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PUM

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Abstract

The invention provides a Cu-ZnO / SiO2 aerogel bimetallic catalyst, as well as a preparation method and application of the Cu-ZnO / SiO2 aerogel bimetallic catalyst. The preparation method comprises the following steps: weighing a SiO2 aerogel, adding the SiO2 aerogel into deionized water, stirring evenly at the constant temperature, dropwise adding a mixed aqueous solution of Cu(NO3)2.3H2O and Zn(NO3)2.6H2O; dropwise adding a Na2CO3 solution, stabilizing the pH value to 7.3-7.7; filtering, washing with the deionized water, drying overnight, roasting, tableting a sample, screening, and preparing a catalyst parent; conducting pretreatment of reduction activation on the catalyst parent in mixed gases of nitrogen and hydrogen, raising the temperature to 240 DEG C through a program at the speed of 2 DEG C per minute at the pressure of 0.1 MPa, wherein the volume fraction of H2 is 10%; raising the temperature to 300 DEG C through a program at the speed of 1.0 DEG C per minute, regulating the volume fraction of H2 to 30%, reducing for 6 hours at the constant temperature of 300 DEG C to obtain the reduced catalyst, namely the Cu-ZnO / SiO2 aerogel bimetallic catalyst. The distinguishing characteristic of the Cu-ZnO / SiO2 aerogel bimetallic catalyst and the preparation method is that the preparation process of the adopted SiO2 aerogel bimetallic catalyst is simple, and the SiO2 aerogel bimetallic catalyst is excellent in catalytic activity and stability in the reaction process.

Description

technical field [0001] The present invention relates to a kind of Cu-ZnO / SiO 2 The airgel bimetallic catalyst and its preparation method and application belong to the field of organic catalysis. Background technique [0002] As an organic chemical product, the output of methanol is second only to basic raw materials such as ethylene, propylene and pure benzene in the world. There are many derivatives of methanol, which are used to manufacture various organic products such as formaldehyde, acetic acid, dimethyl ether, low-carbon olefins, methyl chloride, methylamine, etc. It is also one of the important raw materials for pesticides and medicines, so it is called C 1 The basis of chemistry. The world's methanol production is dominated by natural gas. my country is a country rich in coal, poor in gas and little in oil. Coal is the main raw material for methanol production. In recent years, foreign methanol has a strong cost advantage. Due to the rise in international oil and...

Claims

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Application Information

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IPC IPC(8): B01J23/80C07C67/40C07C69/06
CPCC07C67/40B01J23/80B01J35/23C07C69/06
Inventor 胡靖王爱丽殷恒波贾星原
Owner JIANGSU UNIV
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