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Preparation method of methanol synthesis catalyst

A technology for synthesizing methanol and catalysts, which is applied in the preparation of organic compounds, chemical instruments and methods, preparation of hydroxyl compounds, etc. It can solve the problems affecting the physical and chemical properties of catalysts and the dispersion effect of active components is not obvious.

Active Publication Date: 2020-03-31
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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  • Preparation method of methanol synthesis catalyst
  • Preparation method of methanol synthesis catalyst
  • Preparation method of methanol synthesis catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0034] Cu(NO 3 ) 2 ·3H 2 O, Zn(NO 3 ) 2 ·6H 2 O was dissolved in deionized water to form a 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 1.0 hour to obtain slurry I. The slurry I was aged under stirring, the stirring speed was 200 rpm, the aging temperature was 75° C., the pH value was 7.0, 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 parallel, the molar ratio of the amount of sodium carbonate to the total amoun...

Embodiment 2

[0036] 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 to form a mixed solution A, and 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 3 45g / L) and the mixed solution A were added into the reaction tank concurrently, the gelling temperature was 55°C, the gelling pH was 7.2, and the gelling time was 0.8 hours to obtain slurry I. The slurry I was aged under stirring, the stirring speed was 210 rpm, the aging temperature was 72° C., the aging pH value was 6.8, and the aging was 0.5 hours. After aging, the mixed solution B and sodium carbonate solution are added into the slurry I in parallel, the molar ratio of the amount of sodium carbonate to the total amount of copper and zinc is 2.4, the gelling tem...

Embodiment 3

[0038] 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 to form a mixed solution A, 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 52g / L) and mixed solution A were added into the reaction tank in parallel, the gelation temperature was 45°C, the pH value was 7.8, and the gelation time was 1.2 hours to obtain slurry I. The slurry I was aged under stirring, the stirring speed was 230 rpm, the aging temperature was 73° C., the aging pH value was 7.1, and the aging time was 0.6 hours. After the aging is finished, the mixed solution B and the sodium carbonate solution are added into the slurry I in parallel, the molar ratio of the amount of sodium carbonate to the total amount of copper and zin...

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Abstract

The invention discloses a preparation method of a methanol synthesis catalyst. The preparation method comprises the following steps: (1) carrying out a parallel flow gelling reaction on a mixed solution A and a sodium metaaluminate solution to obtain a slurry I, and aging; (2) adding a mixed solution B and a sodium carbonate solution into the aged slurry I obtained in the step (1) in a dropwise and parallel flow manner, carrying out a gelling reaction to obtain a slurry II, and aging; and (3) carrying out solid-liquid separation on the material obtained in the step (2), and drying, roasting and molding the solid phase to obtain the catalyst, wherein the mixed solution A is an aqueous solution containing a soluble copper salt and a soluble zinc salt, and the mixed solution B is an aqueous solution containing a soluble copper salt and a soluble aluminum salt. The catalyst prepared by the method has the advantages of uniform distribution of active metal copper and auxiliary agent zinc, good synergistic effect, large number of active metal active centers, improved activity, improved selectivity, improved thermal stability and prolonged service life.

Description

technical field [0001] The invention relates to a method for preparing a catalyst for synthesizing methanol, in particular to a method for preparing a catalyst for synthesizing methanol 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, temperat...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/80B01J35/10C07C29/154C07C31/04
CPCB01J23/002B01J23/80C07C29/154B01J2523/00B01J35/643B01J35/633B01J35/647B01J35/615B01J2523/17B01J2523/27B01J2523/31C07C31/04Y02P20/52
Inventor 王海涛徐学军王继锋刘东香
Owner CHINA PETROLEUM & CHEM CORP
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