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Copper-manganese base high temperature transformation catalyst and preparation method thereof

A high-temperature shift, catalyst technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc. problems, to achieve the effect of improving heat resistance and low temperature activity, improving low temperature activity, and eliminating side reactions

Inactive Publication Date: 2005-08-17
INNER MONGOLIA UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, except that there is environmental pollution in iron-chromium series catalysts, the main technical problem in use is that a large amount of excess water vapor is needed to prevent the active components (Fe 3 o 4 ) is excessively reduced, resulting in a reduction in catalyst activity, and more seriously, a series of side reactions such as Fischer-Tropsh (Fischer-Tropsch reaction) occur, so that it cannot meet the requirements of new energy-saving processes
Even the improved iron-chromium high-temperature shift catalyst has a certain limit to the ability to resist the side reaction of Fischer-Tropsh (Fischer-Tropsch reaction). 2 O / CO) will still produce a large amount of F-T side reaction products under the lower conditions, causing a series of serious consequences, such as the reduction of hydrogen production, the poisoning of low shift catalyst, the deterioration of operating state, etc., so the elimination of Fischer-Tropsh side reaction The fundamental approach is to develop iron-free catalysts
[0003] The earliest reports on the research of non-iron-based high-temperature shift catalysts to overcome the problem of Fischer-Tropsh side reactions in iron-based high-temperature shift catalysts are the Cu-based shift catalysts LK-811 and KK142 reported by Topsoe, Denmark. The highest heat-resistant temperature is about 350°C-390°C, although it is much higher than the heat-resistant temperature of Cu-Zn low-temperature shift catalyst (250°C), but compared with the heat-resistant temperature of iron-based high-temperature shift catalyst (480-500°C), There is still a certain gap in its heat resistance

Method used

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  • Copper-manganese base high temperature transformation catalyst and preparation method thereof
  • Copper-manganese base high temperature transformation catalyst and preparation method thereof

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Experimental program
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Effect test

Embodiment 1

[0021] Embodiment 1 prepares 40 grams of copper-manganese-based catalysts

[0022] (a) preparation of copper, manganese aqueous solution

[0023] Weigh CuSO 4 ·5H 2 O 45.1 g, MnSO 4 ·H 2 O is 61.1 grams, mix it and put it into a 2000ml beaker to make a 1200ml mixed solution, put the mixed solution on the electric furnace, heat it to 45°C while stirring, keep the stirring rate at about 240 rpm, and then keep the temperature at 30 minutes to mix thoroughly.

[0024] (b) Preparation of copper-manganese-based catalyst precursor

[0025] Weigh 48 grams of NaOH to make a solution of 300ml, and then transfer it to a spherical funnel. Weigh Al 2 o 3 0.8 g, CeO 2 0.8 g, Al 2 o 3 , CeO 2 Grind the solid particles into powder with a particle size of 60-80 mesh; drop the NaOH solution into the copper-manganese aqueous solution at a rate of about 10ml / min, observe the change of the pH value while adding the ground Al 2 o 3 , CeO 2 Powder, stop dropping when the pH value is...

Embodiment 2

[0037] Embodiment 2 prepares 10 grams of copper-manganese-based catalysts

[0038] (a) preparation of copper-manganese aqueous solution

[0039] Weigh Cu(NO 3 )·3H 2 O 10.0 g, MnSO 4 ·H 2 O is 15.3 grams, mix it and put it in a 2000ml beaker to make a 500ml mixed solution, put the mixed solution on the electric furnace, heat it to 45°C while stirring, keep the stirring rate at about 240 rpm, and then keep the temperature at 30 minutes to fully dissolve.

[0040] (b) Preparation of copper-manganese-based catalyst precursor

[0041] Weigh 15 grams of KOH to make a solution of 75ml, and then transfer it to a spherical funnel. Weigh CeO 2 0.3 g, CeO 2 Grind the solid particles into powder with a particle size of 80-100 mesh; drop the NaOH solution into the copper-manganese aqueous solution at a rate of about 8ml / min, observe the change of the pH value while adding the ground CeO 2 Powder, when the pH value is constant at 10, stop adding dropwise, and then boil it at a te...

Embodiment 3

[0053] Example 3 Preparation of 100 grams of copper-manganese-based high-temperature shift catalyst

[0054] (a) preparation of copper-manganese aqueous solution

[0055] Weigh CuSO 4 ·5H 2 O 110 g, Mn(NO 3 ) 2 ·6H 2 O 300 grams, mix it and put it in a 3000ml beaker to make a 1200ml mixed solution, put the mixed solution on the electric stove, heat it to 45°C while stirring, keep the stirring rate at about 240 rpm, and then keep the temperature for 30 minutes , to fully dissolve it.

[0056] (b) Preparation of copper-manganese-based catalyst precursor

[0057] Weigh 110 grams of NaOH to make a solution of 800ml, and then transfer it to a spherical funnel. Weigh Al 2 o 3 4.8 g, Al 2 o 3 Grind solid particles into powder with a particle size of 80-100 mesh; drop the NaOH solution into the copper-manganese aqueous solution mixture at a rate of about 30ml / min, observe the change of pH value while adding the ground Al 2 o 3 Powder, stop dropping when the pH value is c...

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Abstract

The present invention discloses one kind of Cu-Mn base high temperature conversion catalyst and its preparation process. The catalyst has the general expression of CuaMnbO4-M, where an is 1.0-1.5, b is 1.5-2.0, CuaMnbO4 is the active component and accounts for 95-98 wt%, and M is the heat stabilizing assistant and accounts for 2-5 wt%. The preparation process of the catalyst includes compounding water solution containing Cu and Mn, preparing precursor for the catalyst, preparing mixed Cu-Mn precipitate, preparing Cu-Mn base catalyst and other steps. The said process is simple and low in cost, and the preparation catalyst has high heat resistance and high low temperature activity.

Description

technical field [0001] The invention relates to a high-temperature shift catalyst, in particular to a copper-manganese-based high-temperature shift catalyst and a preparation method thereof. Background technique [0002] The CO shift reaction plays an important role in hydrogen production and purification of synthesis gas. Since the industrial application of this reaction in 1921, iron-chromium-based high-temperature shift catalysts have been playing an important role. This type of catalyst has the advantages of wide active temperature, good thermal stability, and strong anti-toxic performance. Its basic composition has changed little over the years. However, except that there is environmental pollution in iron-chromium series catalysts, the main technical problem in use is that a large amount of excess water vapor is needed to prevent the active components (Fe 3 o 4 ) is excessively reduced, resulting in a reduction in catalyst activity, and more seriously, a series of si...

Claims

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Application Information

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IPC IPC(8): B01J23/889C01B3/16
CPCY02P20/52
Inventor 刘全生何润霞崔协力张前程牟占军
Owner INNER MONGOLIA UNIV OF TECH