Preparation method of catalyst for reforming of methane and carbon dioxide to prepare syngas

A carbon dioxide and catalyst technology, which is applied in the field of preparation of a supported nickel-based catalyst for the reforming of methane and carbon dioxide to syngas, can solve the problems of accelerating the deep oxidation of the product, increasing the cost of the catalyst, and making little contribution of the catalyst, and improving the conversion rate and the product. selectivity, avoid further oxidation, reduce catalyst cost

Active Publication Date: 2016-06-08
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 reforming of methane and carbon dioxide to prepare syngas

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0030] Weigh 2.97g of nickel nitrate and 1.98g of cobalt nitrate and dissolve them in an appropriate amount of deionized water to obtain solution A; use an equal volume impregnation method to load 20g of alumina (pore volume 0.72ml / g, specific surface area 242m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 4h, dried at 80°C for 12h, and calcined at 700°C for 4h to prepare catalyst precursor B, in which Ni accounted for 3% of the weight of the carrier by element and Co by element Accounting for 2% of the weight of the carrier; catalyst precursor B is activated in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450 ° C, 0.2 MPa (absolute pressure), and the reduction time is 4 hours; after the reduction activation The catalyst precursor B and 300mL of sorbitol solution with a mass concentration of 10% were added to the autoclave, sealed and replaced with hydrogen for 3 t...

Embodiment 2

[0032] Weigh 2.97g of nickel nitrate and 1.98g of cobalt nitrate and dissolve them in an appropriate amount of deionized water to obtain solution A; use equal volume impregnation method to load 20g of silicon oxide (pore volume is 1.06ml / g, specific surface area is 387m 2 / g, spherical, equivalent diameter 0.5mm) carrier, aged at room temperature for 4h, dried at 80°C for 12h, and calcined at 700°C for 4h to obtain catalyst precursor B, in which Ni accounted for 3% of the weight of the support as an element, and Co accounted for The weight of the carrier is 2%; the catalyst precursor B is activated in a mixed atmosphere containing hydrogen. Catalyst precursor B and 300mL sorbitol solution with a mass concentration of 10% were added to the autoclave, sealed and replaced with hydrogen for 3 times, then adjusted the hydrogen pressure to 3MPa, and reacted at 220°C for 4h; After the mixture was placed for 2h, filtered, the resulting solid sample was dried at room temperature until ...

Embodiment 3

[0034] Weigh 2.97g of nickel nitrate and 1.98g of cobalt nitrate and dissolve them in an appropriate amount of deionized water to obtain solution A; use equal volume impregnation method to load 20g of SBA-15 (pore volume is 1.23ml / g, specific surface area is 701m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 4h, dried at 80°C for 12h, and calcined at 700°C for 4h to prepare catalyst precursor B, in which Ni accounted for 3% of the weight of the carrier by element and Co by element Accounting for 2% of the weight of the carrier; catalyst precursor B is activated in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 80%, the reduction condition is 450 ° C, 0.2 MPa (absolute pressure), and the reduction time is 4 hours; after the reduction activation The catalyst precursor B and 300mL of sorbitol solution with a mass concentration of 10% were added to the autoclave, sealed and replaced with hydrogen for ...

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Abstract

The invention provides a preparation method of a catalyst for reforming of methane and carbon dioxide to prepare syngas. The catalyst comprises an active component, a first auxiliary agent, a second auxiliary agent, and a carrier. The preparation method comprises the following steps: dissolving an active component precursor and a first auxiliary agent precursor into water to obtain a solution (A); then adding a carrier, carrying out aging, drying, and burning to obtain a catalyst precursor (B); reducing the catalyst precursor (B) in a reducing atmosphere; adding the reduced catalyst precursor (B) and a polyol solution into a reactor to carry out hydrogenation reactions, collecting the effluent, filtering, and drying to obtain a catalyst precursor (C); adding an active component precursor and a second auxiliary agent precursor into water to obtain a solution (D), then adding the catalyst precursor (C), drying, and burning to obtain the catalyst. The provided preparation method has the advantages that more active components are dispersed on the surface of carriers, the utilization rate of active metal is improved therefore, and at the same time, the methane conversion rate and product selectivity are both improved.

Description

technical field [0001] The invention relates to a preparation method of a catalyst for producing synthesis gas by methane carbon dioxide reforming, in particular to a preparation method for a supported nickel-based catalyst for producing synthesis gas by methane carbon dioxide reforming. 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 metal catal...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J29/035B01J23/78B01J23/83C01B3/40
CPCY02P20/52
Inventor 孙晓丹张舒冬张信伟刘继华
Owner CHINA PETROLEUM & CHEM CORP
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