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A kind of preparation method of copper-zinc base hydrogenation catalyst

A hydrogenation catalyst, copper-zinc technology, applied in the direction of catalyst activation/preparation, chemical instruments and methods, metal/metal oxide/metal hydroxide catalyst, etc., can solve the problems of uneconomical and environmental protection, and achieve high BET Effect of specific surface area, high activity, and high activity copper specific surface area

Active Publication Date: 2019-02-22
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, the former is washed with organic solvents, which is not economical and environmentally friendly; the latter is washed after one calcination, which does not avoid the adverse effects on the formation of the catalyst structure during the heat treatment process caused by the presence of sodium.

Method used

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

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Experimental program
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Effect test

Embodiment 1

[0021] Weigh 36.24 grams of copper nitrate trihydrate and 104.12 grams of zinc nitrate hexahydrate and dissolve them in 2000 mL of deionized water to obtain a copper-zinc mixed solution. In the sample preparation bucket of deionized water, and the pH of the solution in the bucket was controlled to be 7, and the primary precipitate was obtained after filtration; the primary precipitate was first washed with water, each time with 1000mL of 20°C deionized water, washed 8 times in total, and then used for 5 ℃, 5% ammonium carbonate aqueous solution for washing, each washing with 800mL ammonium carbonate solution, stirring and washing for 5min, washing once in total, after filtering, a secondary precipitate containing copper and zinc was obtained; the secondary precipitate was heated at 70°C Dry overnight, after drying, the sample is dispersed into 800mL deionized water and stirred for 5min, after filtration, the final precipitate containing copper and zinc is obtained; the final pr...

Embodiment 2

[0025] Weigh 48.32 grams of copper nitrate trihydrate and 89.24 grams of zinc nitrate hexahydrate and dissolve them in 1500 mL of deionized water to obtain a copper-zinc mixed solution. 200mL deionized water sample preparation bucket, and control the pH of the solution in the bucket to 8, and obtain the primary precipitate after filtration; the primary precipitate is first washed with water, each time with 40 ℃ deionized water 1000mL, a total of 8 times of washing, and then used Wash with 3% ammonium carbonate aqueous solution at 20°C, use 600mL ammonium carbonate solution for each wash, stir and wash for 5min, and wash once in total. After filtration, a secondary precipitate containing copper and zinc is obtained; ℃ dried overnight, after drying, the sample was dispersed into 800mL deionized water and stirred for 5min, and the final precipitate containing copper and zinc was obtained after filtration; the final precipitate was mixed with 4.03 grams of Al 2 o 3 The powders we...

Embodiment 3

[0029] Weigh 60.4 grams of copper nitrate trihydrate and 74.37 grams of zinc nitrate hexahydrate and dissolve them in 1500 mL of deionized water to obtain a copper-zinc mixed solution. 200mL deionized water sample preparation barrel, and control the pH of the solution in the barrel to 7.5, and obtain the primary precipitate after filtration; the primary precipitate is first washed with water, each time with 60 ℃ deionized water 1000mL, washed 8 times in total, and then used 30°C, 1% by mass ammonium bicarbonate aqueous solution, 800mL of ammonium carbonate solution for each washing, stirring and washing for 5min, washing twice in total, after filtration, a secondary precipitate containing copper and zinc was obtained; the secondary precipitate was in Dry overnight at 90°C. After drying, the sample is dispersed in 800 mL of deionized water and stirred for 5 minutes. After filtration, the final precipitate containing copper and zinc is obtained; the final precipitate is mixed wit...

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Abstract

The invention relates to a preparation method of a copper-zinc-based hydrogenation catalyst and belongs to the technical field of catalysts. The method comprises steps as follows: a prepared copper and zinc mixed nitrate aqueous solution is mixed with an alkaline precipitant, the pH and the temperature in the process are controlled, and a primary precipitate is obtained; the primary precipitate is washed with an alkaline ion exchanger aqueous solution easy to pyrolyze after being washed with water, and a secondary precipitate containing zinc and copper is obtained; the secondary precipitate is dried and washed with water, and a final precipitate containing copper and zinc is obtained; the final precipitate containing copper and zinc and a carrier are mixed, pulped and subjected to solid-liquid separation in water, a solid material is dried, roasted and finally formed, and the copper-zinc-based hydrogenation catalyst is obtained finally.

Description

technical field [0001] The invention provides a method for preparing a catalyst with low impurity content, in particular to a method for preparing a copper-zinc-based hydrogenation catalyst, and belongs to the technical field of catalysts. Background technique [0002] Copper-zinc-based catalysts are widely used in industry as hydrogenation catalysts with excellent performance, such as for synthesis gas to methanol, maleic anhydride hydrogenation to γ-butyrolactone, aldehyde hydrogenation to alcohol, etc. The performance of the catalyst is not only related to the formula, but also the preparation method is very important. The preparation method directly affects the physical and chemical properties of the bulk phase and surface of the catalyst, and then affects the catalytic performance of the catalyst in a specific reaction. [0003] At present, most industrial copper-zinc-based catalysts are prepared by co-precipitation method, using cheap sodium carbonate or hydroxide as p...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J37/03B01J35/10B01J21/04B01J23/80
Inventor 于杨殷玉圣魏士新陈海波
Owner CHINA PETROLEUM & CHEM CORP