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A kind of preparation method of copper-zinc catalyst

A catalyst, copper-zinc technology, applied in the field of preparation of copper-zinc catalysts, can solve the problems of affecting the physical and chemical properties of the catalyst, the dispersion effect of active components is not obvious, etc.

Active Publication Date: 2022-03-08
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] The method mentioned above changes the dispersion of copper on the catalyst after reduction by changing the copper-based catalyst preparation process or adding additives on this basis, and improves the activity of the catalyst. In the process of improving the dispersion of copper components, other physical and chemical properties of the catalyst are affected, and the effect of improving the dispersion of active components is not obvious

Method used

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  • A kind of preparation method of copper-zinc catalyst
  • A kind of preparation method of copper-zinc catalyst
  • A kind of preparation method of copper-zinc catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0036] Cu(NO 3 ) 2 ·3H 2 O, Zn(NO 3 ) 2 ·6H 2 O was dissolved in deionized water, added 116 grams of hydroxyethylidene diphosphonic acid and mixed uniformly to prepare mixed solution A, Cu 2+ The concentration is 2.8mol / L, Zn 2+ The concentration is 2.5mol / L. Cu(NO 3 ) 2 ·3H 2 O and AlCl 3 ·6H 2 O was dissolved in deionized water to form a mixed solution B, Cu 2+ Concentration is 1.8mol / L, Al 3+ The concentration is 2.0mol / L. Add deionized water in the reaction tank, sodium metaaluminate solution (containing Al 2 o 3 42g / L) and the mixed solution A were added into the reaction tank concurrently, the gelling temperature was 60°C, the gelling pH was 7.5, and the gelling time was 0.9 hours to obtain slurry I. The slurry I was aged under stirring, the stirring speed was 190 rpm, the aging temperature was 75° C., the pH value was 7.2, and the aging time was 0.7 hours. After aging, the mixed solution B and sodium carbonate solution are added to the aged slurry I in ...

Embodiment 2

[0038] According to the method for embodiment 1, by the component content ratio of catalyst B in table 1, Cu(NO 3 ) 2 ·3H 2 O, Zn(NO 3 ) 2 ·6H 2 O was dissolved in deionized water, added 188 grams of ethylenediamine tetramethylene phosphonic acid and mixed uniformly, and mixed solution A was prepared, and Cu(NO 3 ) 2 ·3H 2 O and Al 2 (SO 4 ) 3 18H 2 O was dissolved in deionized water to form mixed solution B. Add deionized water in the reaction tank, sodium metaaluminate solution (containing Al 2 o 3 54g / L) and the mixed solution A were added into the reaction tank in parallel, the gelation temperature was 55°C, the pH value of the gelation was 7.0, and the gelation time was 0.8 hours to obtain the slurry I. The slurry I was aged under stirring, the stirring speed was 240 rpm, the aging temperature was 76° C., the aging pH value was 7.4, and the aging was 0.6 hours. After aging, the mixed solution B and the sodium carbonate solution are added into the slurry I in...

Embodiment 3

[0040] According to the method for embodiment 1, by the component content ratio of catalyst C in table 1, Cu(NO 3 ) 2 ·3H 2 O, Zn(NO 3 ) 2 ·6H 2 O was dissolved in deionized water, and 195 grams of polyacrylic acid (molecular weight: 3000) and 95 grams of hydroxyethylene diphosphonic acid were added and mixed evenly to prepare mixed solution A. Cu(NO 3 ) 2 ·3H 2 O and Al(NO 3 ) 3 9H 2 O was dissolved in deionized water to form mixed solution B. Add deionized water in the reaction tank, sodium metaaluminate solution (containing Al 2 o 335g / L) and mixed solution A were added into the reaction tank in parallel, the gelation temperature was 48°C, the pH value was 8.0, and the gelation time was 1.3 hours to obtain slurry I. The slurry I was aged under stirring, the stirring speed was 190 rpm, the aging temperature was 78° C., the aging pH value was 7.2, and the aging time was 0.5 hour. After the aging is finished, the mixed solution B and the sodium carbonate solution ...

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Abstract

The invention discloses a preparation method of a copper-zinc catalyst, which includes the following contents: (1) co-flow gelling reaction of mixed solution A and sodium metaaluminate solution to obtain slurry I, and then aging; (2) mixing Solution B and sodium carbonate solution are added dropwise to the aged slurry I in step (1) for gelation reaction to obtain slurry II, and then aged; (3) The material obtained in step (2) is separated from solid and liquid, The solid phase is dried, calcined and shaped to obtain a catalyst; wherein the mixed solution A is an aqueous solution containing soluble copper salts, soluble zinc salts and organic additives, and the mixed solution B is an aqueous solution containing soluble copper salts and soluble aluminum salts. The catalyst active metal copper prepared by the method of the invention is evenly distributed, has good synergistic effect, and has a large number of active metal active centers, thereby improving the activity, selectivity and thermal stability of the synthetic copper-zinc catalyst and the service life of the catalyst.

Description

technical field [0001] The invention relates to a preparation method of a copper-zinc catalyst, in particular to a preparation method of a copper-zinc catalyst with high activity, high selectivity and good heat resistance. Background technique [0002] As a basic chemical raw material and new energy, methanol has been paid more and more attention. It is widely used in organic synthesis, dyes, fuels, medicines, coatings and national defense industries. With the continuous growth of methanol demand and production capacity along with industrial development in recent years, methanol Its position in the national economy is becoming more and more important. Therefore, in order to further promote the development of the methanol industry, its production technology and catalyst performance need to be further improved. [0003] In industry, methanol is generally used to contain H 2 , CO, CO 2 Syngas is produced under certain conditions of pressure, temperature and presence of cataly...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/80B01J35/10C07C29/154C07C31/04
CPCB01J23/80B01J23/002C07C29/154B01J2523/00B01J35/60B01J2523/17B01J2523/27B01J2523/31C07C31/04Y02P20/52
Inventor 王海涛徐学军王继锋刘东香
Owner CHINA PETROLEUM & CHEM CORP
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