Preparation method of nickel-based catalyst based on SBA-15 and application of nickel-based catalyst in SNG preparation

A catalyst and nickel salt technology, which can be used in molecular sieve catalysts, physical/chemical process catalysts, hydrocarbon production from carbon oxides, etc., can solve problems such as unfavorable reactions, easy sintering and agglomeration, and weak interactions, and achieve a simple and easy preparation method. performance, good thermal stability and high catalytic activity

Inactive Publication Date: 2015-04-29
EAST CHINA UNIV OF SCI & TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Although Ni / Al 2 o 3 and Ni / ZrO 2 The catalytic activity is very good, but NiO and A1 2 o 3 The interaction will cause difficulty in catalyst reduction, while Ni / ZrO 2 As the reaction proceeds, the activity of the catalyst will decrease, which is due to the tetragonal ZrO 2 transformed into monoclinic ZrO 2 , is not conducive to the reaction
And ZrO 2 Carrier price ratio Al 2 o 3 and SiO 2 Expensive, easy to agglomerate at high temperature, therefore, less used in CO methanation reaction
while TiO 2 Due to the high cost, the performance needs to be further improved, so it is less used
Although SiO 2 The carrier has a good pore structure and a large specific surface area, but SiO 2 The mechanical strength of the carrier is not high, and the interaction between the metal component and the carrier is not strong, it is difficult to play a synergistic catalytic effect with the active component, and it is easy to sinter and agglomerate in the strong exothermic methanation reaction, and deactivate quickly

Method used

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  • Preparation method of nickel-based catalyst based on SBA-15 and application of nickel-based catalyst in SNG preparation
  • Preparation method of nickel-based catalyst based on SBA-15 and application of nickel-based catalyst in SNG preparation
  • Preparation method of nickel-based catalyst based on SBA-15 and application of nickel-based catalyst in SNG preparation

Examples

Experimental program
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Embodiment 1

[0029] This example is used to illustrate the synthesis gas to methane catalyst and its preparation method provided by the present invention.

[0030] Weigh 1.24g of nickel nitrate hexahydrate and dissolve it in 6ml of deionized water to prepare an aqueous solution of nickel nitrate. Then weigh 1.0g specific surface area is 650m 2 / g mesoporous molecular sieve SBA-15 (the TEM picture is as figure 2 (A) ), the support SBA-15 was impregnated in the aqueous solution of nickel nitrate by equal volume impregnation method at room temperature. Then transfer it to a vacuum oven at room temperature for vacuum impregnation overnight for 8 hours, and then vacuum-dry it at a temperature of 50° C. for 6 hours. The resulting solid product is roasted in a muffle furnace at a temperature of 500°C for 5 hours. After being ground in a mortar, it is filtered with a 100-mesh sieve to obtain a synthesis gas with a nickel loading of 20wt% for preparing methane. Catalyst, recorded as 20%Ni / SBA-1...

Embodiment 2

[0032] This example is used to illustrate the synthesis gas to methane catalyst and its preparation method provided by the present invention.

[0033] Weigh 0.25g of nickel chloride and dissolve it in 6ml of deionized water to prepare an aqueous solution of nickel chloride. Then weigh 1.0g specific surface area is 650m 2 / g mesoporous molecular sieve SBA-15, the carrier SBA-15 is impregnated in nickel chloride aqueous solution at room temperature by equal volume impregnation method. Then it was transferred to a vacuum oven at room temperature for vacuum impregnation overnight for 2 hours, and then it was dried in vacuum at a temperature of 30°C for 5 hours. The resulting solid product is roasted in a muffle furnace at a temperature of 400°C for 1 hour. After being ground in a mortar, it is filtered with a 100-mesh sieve to obtain a synthesis gas with a nickel loading of 10wt% for preparing methane. Catalyst, recorded as 10%Ni / SBA-15(C). The specific surface area of ​​the ca...

Embodiment 3

[0035] This example is used to illustrate the synthesis gas to methane catalyst and its preparation method provided by the present invention. The preparation method of the synthesis gas to methane catalyst of this embodiment is the same as that of Example 2, except that 0.47 g of nickel acetate tetrahydrate is used instead of 0.25 g of nickel chloride in Example 1.

[0036] In this example, a catalyst for producing methane from synthesis gas with a nickel loading of 10wt% was prepared, which was denoted as 10%Ni / SBA-15(A). The specific surface area of ​​the catalyst is 590 m 2 / g, pore volume 1.21cm 3 / g, pore size 7.53nm.

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Abstract

The invention discloses a catalyst for carbon monoxide methanation and application of the catalyst in reaction of methane prepared from synthesis gas. The catalyst is characterized in that a mesoporous molecular sieve SBA-15 is used as a carrier; metal Ni is used as a main active ingredient; based on metallic elements, 100 parts by weight of the catalyst comprise10-30 parts by weight of nickel and the balance being a molecular sieve SBA-15. When the catalyst is prepared, the mesoporous molecular sieve SBA-15 is impregnated in a nickel salt solution, dried in vacuum, and roasted. In the invention, a traditional method, in which aluminium oxide is used as the carrier, for preparing the methanation catalyst is changed, the mesoporous molecular sieve SBA-15 is used as the carrier to prepare the catalyst which is high in catalytic activity, excellent in methane selectivity, and relatively long in catalyst service life, and the prepared catalyst also has the relatively good activity under low temperature; for the catalyst, the CO conversion rate is 100%, the methane selectivity is 96%, and the methane yield is 96% under the best condition, and thus the catalyst has a relatively wide industrial prospect.

Description

technical field [0001] The invention belongs to the technical field of fine chemicals, and in particular relates to the preparation of a supported catalyst and its application in synthesis gas to methane. Background technique [0002] In recent years, with the continuous growth of the world economy, the demand for energy has been increasing, the prices of oil and natural gas have soared, and the problem of global warming has become increasingly serious. With the implementation of domestic sustainable development strategies and environmental protection policies, since the carbon emissions of methane combustion are much lower than that of oil and coal, natural gas, as a high-quality and efficient clean energy, is strongly sought after by the international market, and the natural gas consumption market continues to grow. With the improvement of people's living standards and the increasing demand of industries, the demand for natural gas is increasing. Although my country's an...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/03C07C9/04C07C1/04
Inventor 辛忠陶淼
Owner EAST CHINA UNIV OF SCI & TECH
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