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Preparation method of catalyst for methane reforming with carbon dioxide to synthetic gas

A carbon dioxide and catalyst technology, which is applied in the field of preparation of supported nickel-based catalysts, can solve the problems of low metal utilization in carrier channels, accelerate product deep oxidation, increase catalyst cost, etc., improve conversion rate and product selectivity, and avoid further Oxidation, the effect of accelerating the adsorption and desorption speed

Active Publication Date: 2016-07-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The reaction life of the obtained catalyst is longer, but the preparation process of this method is complicated and the cost is higher
[0007] Although the catalysts prepared by the above-mentioned patented methods have obtained better reaction performance of methane carbon dioxide reforming to synthesis gas, the catalysts all have the problem of high cost, and the reaction of methane carbon dioxide reforming to synthesis gas is still a fast reaction (this kind The rapid reaction is generally carried out under the condition of mass transfer control), and the reaction is completed when the reactant reaches the outer surface of the catalyst, so the inner surface of the catalyst does not contribute much to the target reaction, which results in a lower The metal utilization rate increases the cost of the catalyst, and at the same time accelerates the deep oxidation of the product

Method used

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  • Preparation method of catalyst for methane reforming with carbon dioxide to synthetic gas

Examples

Experimental program
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Effect test

Embodiment 1

[0027] The spent hydrotreating catalyst (MoCo / Al 2 o 3), the oil on the catalyst surface was removed by extraction, dried at 110°C for 8h, and the obtained catalyst was calcined at 450°C for 4h to obtain catalyst precursor A, in which Mo accounted for 9.1wt% by weight of catalyst precursor A in terms of elements, and Co in terms of elements Accounting for catalyst precursor A weight 1.8wt%, Ni accounts for catalyst precursor A weight 3.1wt% in terms of elements, V accounts for catalyst precursor A weight 1.9wt% in terms of elements; 20g catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrogen for 3 times, then adj...

Embodiment 2

[0029] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the catalyst surface was removed by extraction, dried at 110°C for 8h, and the obtained catalyst was calcined at 450°C for 4h to obtain catalyst precursor A, in which Mo accounted for 9.1wt% by weight of catalyst precursor A in terms of elements, and Co in terms of elements Accounting for catalyst precursor A weight 1.8wt%, Ni accounts for catalyst precursor A weight 3.1wt% in terms of elements, V accounts for catalyst precursor A weight 1.9wt% in terms of elements; 20g catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrogen for 3 times, then ad...

Embodiment 3

[0031] The spent hydrotreating catalyst (MoCo / Al 2 o 3 ), the oil on the catalyst surface was removed by extraction, dried at 110°C for 8h, and the obtained catalyst was calcined at 450°C for 4h to obtain catalyst precursor A, in which Mo accounted for 9.1wt% by weight of catalyst precursor A in terms of elements, and Co in terms of elements Accounting for catalyst precursor A weight 1.8wt%, Ni accounts for catalyst precursor A weight 3.1wt% in terms of elements, V accounts for catalyst precursor A weight 1.9wt% in terms of elements; 20g catalyst precursor A is mixed in hydrogen-containing Activation in the atmosphere, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450°C, 0.2MPa (absolute pressure), and the reduction time is 4h; the catalyst precursor A after reduction and activation is mixed with 300mL of sorbitol with a mass concentration of 10% Add the solution into the autoclave, seal it and replace it with hydrogen for 3 times, then ad...

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Abstract

The invention relates to a preparation method of a catalyst for methane reforming with carbon dioxide to synthetic gas. The catalyst comprises an active ingredient, an additive and a carrier. The preparation method is as below: treating a waste residue oil hydrogenation catalyst to prepare a catalyst precursor A; reducing the catalyst precursor A in a reducing atmosphere; adding the reduced catalyst precursor A and a polyol solution into a high pressure reactor, carrying out a hydrogenation reaction, placing a reaction effluent, filtering and dying to obtain a catalyst precursor B; and dissolving an active ingredient precursor and an additive precursor in water to obtain a solution C, then adding the catalyst precursor B, drying and calcining to obtain the catalyst. The method of the present invention not only makes full use of waste residue oil hydrogenation catalyst, saves cost, but also promotes dispersion of more active ingredients on the surface of the carrier. The method improves the utilization of the active metal, and the conversion of methane and selectivity of products.

Description

technical field [0001] The invention relates to a method for preparing a catalyst for producing synthesis gas by reforming methane and carbon dioxide, in particular to a preparation method for a supported nickel-based catalyst for producing synthesis gas by reforming methane and carbon dioxide. Background technique [0002] Methane and carbon dioxide are cheap and resource-rich carbon-containing compounds in nature. Using the reforming reaction of methane and carbon dioxide to produce synthesis gas is of great significance for alleviating the energy crisis and reducing global warming caused by greenhouse gas emissions . The synthesis gas produced by the reforming of methane and carbon dioxide has H 2 The characteristic of / CO≤1 can be applied to Fischer-Tropsch synthesis to produce high value-added chemicals such as higher hydrocarbons. [0003] At present, the catalysts used for the reforming of methane and carbon dioxide to produce synthesis gas are mainly supported meta...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/887C01B3/40
CPCY02P20/52
Inventor 孙晓丹张舒冬张信伟刘继华
Owner CHINA PETROLEUM & CHEM CORP
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