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Preparation method of anti-sintering methanol synthesis catalyst

A methanol synthesis and catalyst technology, applied in the field of catalysis, can solve the problems of poor economy, low single-pass conversion rate of raw materials, and increased circulation volume, etc., and achieve the effects of stable active specific surface, superior anti-sintering ability, and inhibiting sintering behavior.

Active Publication Date: 2019-11-26
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The former can play a positive role to a certain extent, but due to the large number of components, it puts forward higher requirements for the uniformity and quality stability of the catalyst product
In addition, due to the large number of components, there are many synergistic effects, the analysis of the catalyst mechanism and the influence of element composition on the performance of the catalyst, and based on these analysis results, a series of in-depth and systematic studies such as guiding catalyst replacement have brought complexity.
The latter can indeed play a role in improving the heat resistance of the catalyst, and the selectivity of methanol can basically meet the production requirements, but the activity of the catalyst is low, and the single-pass conversion rate of raw materials is low. In production, the circulation volume needs to be increased to meet the production capacity requirements. High energy consumption and poor economy

Method used

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  • Preparation method of anti-sintering methanol synthesis catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Weigh copper nitrate and zinc nitrate according to the copper / zinc molar ratio of 8:1 and dissolve them in deionized water to obtain a copper-zinc solution with a total substance concentration of 1mol / L. L sodium hydroxide solution was added dropwise to the copper-zinc solution until pH=7.0 in the precipitated solution, washed and removed sodium after stirring and aging for 30 minutes, dried overnight at 90°C, and calcined at 250°C for 4h to obtain catalyst precursor a. The specific surface area of ​​precursor a measured by low temperature nitrogen adsorption and desorption technology is 80m 2 / g, weigh 10g of precursor a as the raw material for subsequent steps.

[0024] Take silica sol and aluminum nitrate to prepare 100mL silicon-aluminum mixed solution, so that the total mass of silicon and aluminum elements in the solution is 0.08g, and the molar ratio of silicon / aluminum element is 1:4; immerse 10g of catalyst precursor a in the silicon-aluminum mixed solution 0....

Embodiment 2

[0027] Weigh copper nitrate and zinc nitrate according to the copper / zinc element molar ratio of 7:1 and dissolve them in deionized water to obtain a copper-zinc solution with a total substance concentration of 1mol / L. L sodium carbonate solution was added dropwise to the copper-zinc solution until pH=7.2 in the precipitation solution, after stirring and aging for 30 minutes, it was washed to remove sodium, dried overnight at 100°C, and calcined at 300°C for 3 hours to obtain catalyst precursor a. The specific surface area of ​​precursor a measured by nitrogen adsorption and desorption technology is 60m 2 / g, weigh 10g of precursor a as the raw material for subsequent steps.

[0028] Take silica sol and aluminum nitrate to prepare 100mL silicon-aluminum mixed solution, so that the total mass of silicon and aluminum in the solution is 0.3g, and the molar ratio of silicon / aluminum is 1:3; immerse 10g of catalyst precursor a in the silicon-aluminum mixed solution 1.0mol / L sodium...

Embodiment 3

[0031] Weigh copper nitrate and zinc nitrate according to the copper / zinc molar ratio of 5:1 and dissolve them in deionized water to obtain a copper-zinc solution with a total substance concentration of 1mol / L. L sodium carbonate solution was added dropwise to the copper-zinc solution until pH = 7.2 in the precipitation solution, washed and removed sodium after stirring and aging for 30 minutes, dried overnight at 120°C, and calcined at 350°C for 1 hour to obtain catalyst precursor a. The specific surface area of ​​precursor a measured by nitrogen adsorption and desorption technology is 65m 2 / g, weigh 10g of precursor a as the raw material for subsequent steps.

[0032] Take silica sol and aluminum nitrate to prepare 100mL silicon-aluminum mixed solution, so that the total mass of silicon and aluminum in the solution is 0.61g, and the molar ratio of silicon / aluminum is 1:2; 10g of catalyst precursor a is immersed in the silicon-aluminum mixed solution 1.2mol / L sodium carbona...

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Abstract

The invention belongs to the technical field of catalysis, and particularly relates to a preparation method of an anti-sintering methanol synthesis catalyst. The method comprises the following steps:preparing a catalyst precursor a containing copper oxide and zinc oxide by using a co-precipitation process; covering the catalyst precursor a by a precipitate of silicon and aluminum by a chemical deposition process to obtain a catalyst precursor b; and treating the catalyst precursor b by an auxiliary agent, and performing molding to obtain the catalyst. According to the method provided by the invention, the methanol synthesis catalyst prepared by the method has good thermal stability, especially in a high-temperature methanol synthesis reaction, and the active specific surface area of the catalyst and the methanol yield can be well maintained.

Description

technical field [0001] The invention belongs to the technical field of catalysis, and in particular relates to a preparation method of a sintering-resistant methanol synthesis catalyst. Background technique [0002] With the rapid development of MTO, MTP, MTA and MTG, as well as the downstream product technology of methanol as a raw material for hydrogen production of new energy vehicles, it has driven the great development of the entire methanol industry, and at the same time promoted the development of large methanol technology. Methanol synthesis catalyst is the core technology of methanol production. With the specific application requirements of methanol synthesis feed gas, process and product methanol, many stringent requirements are put forward for methanol synthesis catalyst. Among them, methanol synthesis catalyst needs continuous improvement. The thermal stability of the synthesized catalyst, mainly to improve the anti-sintering performance of the active component m...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/072C07C31/04C07C29/154
CPCB01J29/072C07C31/04C07C29/154Y02P20/52
Inventor 于杨陈海波殷玉圣
Owner CHINA PETROLEUM & CHEM CORP
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