Catalyst for synthesizing methanol and preparation method thereof

A technology for synthesizing methanol and catalysts, applied in catalyst activation/preparation, chemical instruments and methods, preparation of hydroxyl compounds, etc., can solve the problems of high heat sensitivity and rapid activity decline, and achieve the effects of high methanol selectivity and long service life

Active Publication Date: 2009-10-21
SINOPEC NANJING RES INST OF CHEM IND CO LTD
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  • Summary
  • Abstract
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  • Application Information

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Problems solved by technology

CO, CO 2 and H 2 The synthesis of methanol began in 1923. At that time, the high-pressure method (300°C-400°C, 25Mpa-30MPa) was used in the methanol synthesis industry. The catalyst was ZnO / Cr2O3. In the early 1950s, Poland first applied ternary CuO / ZnO / Al 2 o 3 Catalysts for the synthesis of methanol. Compared with ZnO / Cr2O3 catalysts, copper-based catalysts have the characteristics of low temperature, low pressure and high activity, but are highly sensitive to poisons such as sulfur and heat. With the development of gas purification technology and the improvement of thermal stability of catalysts Further improvement, the application of copper-based catalysts entered a new stage of development in the 1960s. In the late 1960s and early 1970s, my country also developed the C207 alcohol catalyst used in my country's unique alcohol process by the Nanhua Group Research Institute. At present, there are many manufacturers producing this type of catalyst, but the production process has not been improved for decades, exposing the characteristics of the catalyst with high initial activity but rapid activity decay

Method used

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  • Catalyst for synthesizing methanol and preparation method thereof
  • Catalyst for synthesizing methanol and preparation method thereof

Examples

Experimental program
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Embodiment 1

[0018] (1) With mixed solution. Take 1.0M Cu(NO 3 ) 2 750ml, 1.0M Zn(NO 3 ) 2 750ml is mixed in a 2000ml beaker.

[0019] (2) neutralization. Take 3000ml 0.25M Na 2 Put the CO solution in a 5000ml beaker and heat it to 80°C, and add the (1) mixture to Na at a rate of 200ml / min under stirring 2 CO 3 In the solution, when the pH=7.2 is the end point, stop heating and stirring after aging for 0.5 hours.

[0020] (3) Washing. After (2) precipitation, wash the precipitate with tilting method (using 70°C deionized water) until there is no NO 3 - .

[0021] (4) Put 12.5g Al(OH) 3 The powder is first activated with 3% boric acid solution, then poured into the precipitate and stirred for 20 minutes.

[0022] (5) Suction filtration, drying at 110°C, crushing, and calcining at 350°C for 2 hours.

[0023] (6) Tablet molding. Add a small amount of graphite and water to the mixed oxide obtained in (4), mix well, and press into tablets. Crushed and sieved into 16 mesh to 40 m...

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Abstract

The invention relates to a catalyst for using CO, CO2, and H2 to composite carbinol, wherein its active components comprise Cu30-70%, Zn30-60%, and Al3-15% at mass percentages; and the catalyst is prepared by share deposit method. The inventive catalyst has high low-temperature activity and high initial activity, while its activity is increased 20-30% after heating, and its service life is prolonged with 2-4 months.

Description

Technical field: [0001] The present invention relates to a method for using CO, CO 2 and H 2 Catalyst for synthesizing methanol and its preparation method. Background technique: [0002] Methanol is an important organic chemical raw material, which is widely used in formaldehyde, ethanol, acetic acid, methyl tert-butyl ether, medicine, pesticides, etc. In recent years, with the development of C1 chemistry, the application fields of methanol have been continuously expanded, and its demand has also been continuously expanded. The development of methanol industry has a good prospect. Initially, methanol was obtained exclusively from wood dry distillation. CO, CO 2 and H 2 The synthesis of methanol began in 1923. At that time, the high-pressure method (300°C-400°C, 25Mpa-30MPa) was used in the methanol synthesis industry. The catalyst was ZnO / Cr2O3. In the early 1950s, Poland first applied ternary CuO / ZnO / Al 2 o 3 Catalysts for the synthesis of methanol. Compared with ZnO...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J37/03B01J23/80C07C29/154C07C31/04
CPCY02P20/52
Inventor 刘金辉仇冬黄金钱曹建平
Owner SINOPEC NANJING RES INST OF CHEM IND CO LTD
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