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Preparation method of catalyst for partial oxidation of methane to prepare syngas

A catalyst and synthesis gas technology, which is applied in the field of preparation of a supported nickel-based catalyst by partial oxidation of methane to synthesis gas, can solve the problems of low catalyst contribution, accelerated product deep oxidation, low metal utilization rate of carrier pores, etc. cost, improved conversion and product selectivity, the effect of avoiding further oxidation

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

[0007] Although the catalysts prepared by the above-mentioned patented methods have obtained good performance in the partial oxidation of methane to synthesis gas reaction, since the reaction is a fast reaction (this fast reaction is generally carried out under the condition of mass transfer control), the reaction The reaction is completed when the material 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 metal utilization rate in the pores of the carrier and accelerates the deep oxidation of the product

Method used

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  • Preparation method of catalyst for partial oxidation of methane to prepare syngas
  • Preparation method of catalyst for partial oxidation of methane to prepare syngas
  • Preparation method of catalyst for partial oxidation of methane to prepare syngas

Examples

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Effect test

Embodiment 1

[0029] (1) Preparation of carrier:

[0030] Weigh 85.28g of cetyltrimethylammonium bromide and 81.95g of citric acid, add 842mL of deionized water to make a mixed solution, add 292.6g of aluminum nitrate to the mixed solution, stir for 2h, and then stir at 70°C Until the gel is formed, the gel is aged at room temperature for 12 hours, then dried at 110°C for 8 hours, and calcined at 700°C for 4 hours to obtain an alumina carrier, in which citric acid: hexadecyltrimethylammonium bromide: aluminum element: The molar ratio of water is: 0.5:0.3:1:60. The nature of the carrier is: the specific surface area is 296m 2 / g, the pore volume is 0.65mL / g, and the average pore diameter is 9.8nm.

[0031] (2) Preparation of catalyst:

[0032]Weigh 1.32g of nickel nitrate and dissolve it in 15.5mL of deionized water to obtain solution A; load it on 20g of prepared alumina carrier by equal volume impregnation method, age at room temperature for 4h, dry at 80°C for 12h, and calcinate at 700...

Embodiment 2

[0034] Weigh 1.32g of nickel nitrate and dissolve it in 19.5mL of deionized water to obtain solution A; use the equal volume impregnation method to load 20g of hydrogen ZSM-5 (silicon-aluminum ratio 50, pore volume of 0.23ml / g, specific surface area of ​​426m 2 / g, strip shape, equivalent diameter 1.5mm) carrier, aged at room temperature for 6h, dried at 110°C for 10h, and calcined at 600°C for 4h to obtain catalyst precursor B, wherein Ni accounted for 1% of the catalyst weight in terms of elements; catalyst precursor B Activate in a mixed atmosphere containing hydrogen, the volume content of hydrogen in the mixed gas is 90%, the reduction conditions are 400°C, 0.2MPa (absolute pressure), and the reduction time is 8h; the mass concentration of the reduced and activated catalyst precursor B and 300mL is Add 10% sorbitol solution into the autoclave, seal it and replace it with hydrogen for 4 times, then adjust the hydrogen pressure to 2MPa, and react at 300°C for 2h; place the r...

Embodiment 3

[0036] (1) Preparation of carrier:

[0037] Weigh 72.2g cetyltrimethylammonium bromide and 69.4g citric acid, add 712mL deionized water to make a mixed solution, add 178mL tetraethyl orthosilicate to the mixed solution, stir for 2h, and then Stir at ℃ until it becomes a gel, age the gel at room temperature for 12h, then dry at 110℃ for 8h, and calcinate at 600℃ for 3h to obtain a silica carrier, in which citric acid: hexadecyltrimethylammonium bromide: The molar ratio of silicon element: water is: 0.5:0.3:1:60. The nature of the carrier is: the specific surface area is 565m 2 / g, the pore volume is 0.68mL / g, and the average pore diameter is 5.2nm.

[0038] (2) Preparation of catalyst:

[0039] Weigh 1.32g of nickel nitrate and dissolve it in 13.5mL of deionized water to obtain solution A; load it on 20g of the prepared silica carrier by equal volume impregnation method, age at room temperature for 8h, dry at 120°C for 6h, and calcinate at 600°C for 4h to obtain the catalyst...

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Abstract

The invention relates to a preparation method of a catalyst for partial oxidation of methane to prepare syngas. The catalyst comprises an active component, an auxiliary agent and a carrier. The preparation method comprises the following steps: dissolving an active component precursor into water to obtain a solution (A), adding a carrier into the solution (A), performing 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, drying to obtain a catalyst precursor (C); adding the catalyst precursor (C) into an active component precursor solution, 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 CO conversion rate and product selectivity are both improved.

Description

technical field [0001] The invention relates to a preparation method of a catalyst for the partial oxidation of methane to synthesis gas, in particular to a preparation method of a supported nickel-based catalyst for the partial oxidation of methane to synthesis gas. Background technique [0002] More than 90% of the composition of natural gas is methane, and the synthesis of fuel and chemicals from methane through synthesis gas is one of the effective ways to utilize natural gas. Compared with the traditional steam reforming method, the partial oxidation of methane to synthesis gas has the advantages of small reaction vessel volume, fast reaction rate, low energy consumption, and the generated synthesis gas is suitable as raw material gas for methanol and Fischer-Tropsch synthesis. In addition, the development of partial methane oxidation technology may replace the strong endothermic steam methane reforming process for the production of synthesis gas, especially for the uti...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J29/46
Inventor 孙晓丹张舒冬张信伟刘继华
Owner CHINA PETROLEUM & CHEM CORP
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