Preparation method and application of MgO (111) load nickel-base catalyst

A catalyst and nickel-supported technology, applied in chemical instruments and methods, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc., can solve the problem of catalyst bed pressure rise, insufficient stability, and catalyst Deactivation and other problems, to achieve the effect of prolonging catalyst life, preventing sintering, and resisting carbon deposition

Inactive Publication Date: 2012-09-12
SOUTH CENTRAL UNIVERSITY FOR NATIONALITIES
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

This patented technology has several benefits compared to previous methods such as adding specific structures or modifying existing ones. It also includes strong interactions between different materials like iron (II), manganese (III)) cathode material, magnesium hydroxyl group donors, etc., which helps improve its effectiveness over time without losing their original properties during use.

Problems solved by technology

This patented technical solution discusses various ways to improve the efficiency or performance of traditional methods involving reactants like hydrogen gas production from natural sources through processes that use fossil fuels. However, these techniques often result in emissions containing harmful pollutants which may affect global environmental quality. Non-polluting transition materials based on iron carbides could provide an alternative approach without causing negative effects associated with expensive precious metallic catalyst systems.

Method used

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  • Preparation method and application of MgO (111) load nickel-base catalyst
  • Preparation method and application of MgO (111) load nickel-base catalyst
  • Preparation method and application of MgO (111) load nickel-base catalyst

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Embodiment 1

[0026] Embodiment 1, 2 is the embodiment prepared by MgO(111) supported nickel-based catalyst;

[0027] Embodiment 3, 4 is the embodiment that the catalyst prepared by investigating embodiment 1, 2 is used for methane carbon dioxide reforming reaction activity under different temperatures;

Embodiment 5

[0028] Example 5 is an example of the service life of the catalyst prepared in Example 1 for the carbon dioxide reforming reaction of methane at 750° C.;

Embodiment 6

[0029] Example 6 (comparative example) is an example for investigating the service life of commercial MgO-supported nickel-based catalysts for the carbon dioxide reforming reaction of methane catalyzed at 750°C.

[0030] Example 1

[0031] A preparation method of MgO(111) supported nickel-based catalyst, the steps are as follows:

[0032] (1) Synthesis of MgO(111) carrier:

[0033] Dissolve 3.6g of magnesium strips in 159mL of anhydrous methanol, then add 10.36g of structure-directing agent p-methoxybenzyl alcohol, stir for 5h, then add water-in-methanol solution (formed by mixing 5.4g of water and 110mL of methanol) dropwise ), stirring at the same time to make the magnesium methoxide hydrolyze, continue to stir for 12h after the dropwise addition, then put it into a high-pressure reactor, first feed argon to exhaust the air in the kettle, and then continue to feed argon until the pressure in the kettle is 1.0MPa , heated to 265°C and reacted under supercritical conditions ...

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Abstract

The invention belongs to a catalyst preparation technology field of reforming methane with carbon dioxide to produce synthesis gas, and particularly discloses a preparation method and application of MgO (111) load nickel-base catalyst. The catalyst is synthesized by a step of carrier synthesis and a step of Ni/MgO (111) preparation. The carrier is prepared by dissolving magnesium ribbon into a absolute methanol, adding anisyl alcohol and stirring, adding a water methanol solution dropwise under stirring, putting the hydrolyzed mixture into a high pressure reactor, leading argon into the reactor to replace the atmosphere, and then pressurizing to 1.0 MPa, reacting at the temperature of 265 DEG C, cooling and putting the obtained product into a tubular furnace, and calcinating the product; and the Ni/MgO (111) is prepared by immersing the carrier in an acetylacetone nickel solution uniformly, and calcinating for 5 h at the temperature of 650 DEG C after drying. The results of using the catalyst for catalyzing the reforming reaction of methane and carbon dioxide show that the catalyst has good activity and stability and enables the conversion rate of both CH4 and CO2 to be over 85%, and that the catalyst activity can stably maintain for 200 h without obvious inactivation.

Description

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Claims

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Application Information

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Owner SOUTH CENTRAL UNIVERSITY FOR NATIONALITIES
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