Preparation method of high-temperature-resistant methanation catalyst

A methanation catalyst and high temperature resistant technology, applied in catalyst activation/preparation, carbon compound catalysts, catalysts, etc., can solve the problems of easy sintering of active components, easy deactivation of carbon deposits, easy breakage, etc., and achieve good anti-sintering ability. , the effect of improving catalyst strength and reducing fluidity

Active Publication Date: 2018-03-13
XIAN SUNWARD AEROSPACE MATERIAL CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The preparation method is simple and novel, and a methanation catalyst with high activity and high strength is prepared. The nickel content in the catalyst is low, and the preparation cost is low, but the catalyst has high activity, strong anti-coking ability, stable activity during long-term use, and is not broken. It solves the problems that the active components of the existing high-temperature methanation catalysts are easy to sinter, easy to deactivate due to carbon deposition, and easy to break after long-term use

Method used

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  • Preparation method of high-temperature-resistant methanation catalyst
  • Preparation method of high-temperature-resistant methanation catalyst
  • Preparation method of high-temperature-resistant methanation catalyst

Examples

Experimental program
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Effect test

Embodiment 1

[0027]Dissolve 38.9g nickel nitrate hexahydrate and 2.5g aluminum nitrate nonahydrate in 1300mL water to prepare a mixed solution; in addition, dissolve 15.3g sodium carbonate in 1400mL water, add the mixed solution into the sodium carbonate solution at 25°C and stir for precipitation Reaction: After the precipitation reaction is finished, add 0.5g of tetramethoxysilane and stir evenly, then add 115.3g of pseudo-boehmite, stir and mix evenly, then filter and wash with water for several times and then dry at 80°C for 5h to remove water, and the dried material is calcined at 320°C for 10 hours, then mixed with graphite and pressed into tablets to obtain a finished high-temperature-resistant methanation catalyst.

[0028] In this embodiment, the finished high-temperature-resistant methanation catalyst is composed of the following raw materials in mass percentages: 10% nickel oxide, 89% aluminum oxide, 0.2% silicon dioxide, and the balance is graphite.

Embodiment 2

[0030] Dissolve 63.6g of nickel chloride hexahydrate and 7.1g of aluminum chloride in 750mL of water; in addition, dissolve 36.9g of sodium carbonate in 1000mL of water, add nickel chloride and aluminum chloride solution into the sodium carbonate solution at 25°C for precipitation After the precipitation is complete, add 1.7g of tetraethoxysilane and stir evenly, then add 99.7g of boehmite, stir and mix evenly, then filter and wash with water for several times and then dry at 80°C for 5h to remove water. After drying, the material is in Calcined at 380°C for 5 hours, then mixed with graphite and pressed into tablets to obtain a finished high temperature resistant methanation catalyst.

[0031] In this embodiment, the finished high-temperature-resistant methanation catalyst is composed of the following raw materials in mass percentage: 20% nickel oxide, 78.5% aluminum oxide, 0.5% silicon dioxide, and the balance is graphite.

Embodiment 3

[0033] Dissolve 100.0g nickel acetate and 120.5g aluminum nitrate nonahydrate in 500mL water; in addition, dissolve 122.0g potassium carbonate in 1000mL water, add nickel nickel acetate and aluminum nitrate solution to potassium carbonate solution at 50°C for precipitation; precipitation is complete Finally, add 11.7g of silica sol with 20% solid content and stir evenly, then add 62.0g of aluminum hydroxide, stir and mix evenly, then filter and wash with water for several times, then dry at 80°C for 5h to remove water, and dry the material at 450°C Calcined at lower temperature for 2 hours, then mixed with graphite and pressed into tablets to obtain a finished product of high temperature resistant methanation catalyst.

[0034] In this embodiment, the finished high-temperature-resistant methanation catalyst is composed of the following raw materials in mass percentage: 30% nickel oxide, 61% aluminum oxide, 5% silicon dioxide, and the balance is graphite.

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Abstract

The invention discloses a preparation method of a high-temperature-resistant methanation catalyst. The method comprises the following steps of firstly dissolving a soluble nickel salt and a soluble aluminum salt in deionized water, confecting to form a mixed solution, afterwards, adding a precipitator into the solution, carrying out a precipitation reaction in a condition that a temperature is 25to 90 DEG C, after the precipitation reaction is finished, adding a silicon reagent and hydrated alumina in sequence, uniformly agitating and mixing, then carrying out filtration, washing, drying andcalcination in sequence, finally, mixing graphite, and carrying out press forming to obtain a finished product of the methanation catalyst. The method provided by the invention is simple and novel; the methanation catalyst which is high in activity and high in strength is prepared; the nickel content in the catalyst is low; the preparation cost is low; however, the catalyst is high in activity andhigh in carbon deposition resisting ability, is stable in activity in a long-time use process and is not crushed and problems that an existing high-temperature-resistant methanation catalyst is easyto sinter in active component, is easy in carbon deposition to be inactivated and is easy to crush when being used for a long time are solved.

Description

technical field [0001] The invention belongs to the technical field of catalyst preparation, and in particular relates to a preparation method of a high-temperature-resistant methanation catalyst. Background technique [0002] With the continuous development of my country's economy, the demand for energy is increasing. The remarkable feature of my country's energy structure is "rich in coal, poor in oil, and low in gas". Natural gas resources as a clean fuel are scarce, and a large amount of natural gas needs to be imported every year. It is estimated that by 2020, the demand for natural gas will exceed 300 billion m 3 , the market gap will reach 90 billion m 3 . Therefore, the development of coal-to-gas can not only alleviate the serious environmental pollution problem in my country, but also alleviate the shortage of natural gas supply in my country and improve the energy structure. [0003] The core process for developing coal-to-gas is the methanation process, and th...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J37/03B01J37/08C07C1/04C07C9/04
CPCB01J23/002B01J23/755B01J37/031B01J37/086B01J2523/00C07C1/0435C07C2523/755B01J2523/31B01J2523/41B01J2523/847C07C9/04
Inventor 许龙龙王胜雷侯亚楠彭东封超于阳
Owner XIAN SUNWARD AEROSPACE MATERIAL CO LTD
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