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A kind of preparation method of synthetic gas methanation catalyst

A catalyst and gas methane technology, which is applied in the field of preparation of a supported nickel-based catalyst for the methanation of synthesis gas, can solve the problems of low metal utilization rate of carrier pores, increased catalyst preparation cost, and little contribution to the target reaction of the catalyst, and achieves improved conversion. rate and product selectivity, avoid further conversion, and accelerate the effect of adsorption and desorption

Active Publication Date: 2018-02-09
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] Although the catalysts prepared by the above-mentioned patented methods have obtained better synthesis gas methanation reaction performance, because the reaction is a fast reaction (this kind of fast reaction is generally carried out under the condition of mass transfer control), the reactants in The reaction is completed when it 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 lower metal utilization in the carrier pores and increases the preparation cost of the catalyst

Method used

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  • A kind of preparation method of synthetic gas methanation catalyst
  • A kind of preparation method of synthetic gas methanation catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0026] Mix an appropriate amount of n-octane, n-hexanol and Tween 80 to make a stable microemulsion. Add an aqueous solution containing an appropriate amount of nickel nitrate and ammonium molybdate to the microemulsion, stir well at 40°C, and then add an appropriate amount of 60% Hydrazine hydrate solution, after stirring for 5 hours, add an appropriate amount of alumina (the pore volume is 0.71ml / g, the specific surface area is 236m 2 / g) Carrier, after stirring for 2h at 80℃, filter, the solid precipitate obtained is washed 4 times with ethanol, then dried at 110℃ for 5h, calcined at 450℃ for 6h, to prepare catalyst precursor A, Ni is calculated as element The weight of the carrier is 3%, and Mo accounts for 2% of the weight of the carrier based on elements; n-octane: n-hexanol: Tween 80: active component nickel: first auxiliary molybdenum = 0.8:1:0.3:2.4:1, hydrazine hydrate The volume ratio of solution to n-octane is 1:35.

[0027] Activate 20g of catalyst precursor A in a m...

Embodiment 2

[0029] Mix an appropriate amount of n-octane, n-hexanol and Tween 80 to make a stable microemulsion. Add an aqueous solution containing an appropriate amount of nickel nitrate and ammonium molybdate to the microemulsion, stir well at 40°C, and then add an appropriate amount of 60% Hydrazine hydrate solution, after stirring for 5 hours, add an appropriate amount of hydrogen type ZSM-5 (silica to aluminum ratio of 50, pore volume of 0.23ml / g, specific surface area of ​​426m 2 / g) Carrier, after stirring for 2h at 80℃, filter, the solid precipitate obtained is washed 4 times with ethanol, then dried at 110℃ for 5h, calcined at 450℃ for 6h, to prepare catalyst precursor A, Ni is calculated as element The weight of the carrier is 3%, and Mo accounts for 2% of the weight of the carrier based on elements; n-octane: n-hexanol: Tween 80: active component nickel: first auxiliary molybdenum = 0.8:1:0.3:2.4:1, hydrazine hydrate The volume ratio of solution to n-octane is 1:35.

[0030] Activ...

Embodiment 3

[0032] Mix an appropriate amount of n-octane, n-hexanol and Tween 80 to make a stable microemulsion. Add an aqueous solution containing an appropriate amount of nickel nitrate and ammonium molybdate to the microemulsion, stir well at 40°C, and then add an appropriate amount of 60% Hydrazine hydrate solution, after stirring for 5 hours, add an appropriate amount of silica (pore volume is 1.06ml / g, specific surface area is 387m 2 / g) Carrier, after stirring for 2h at 80℃, filter, the solid precipitate obtained is washed 4 times with ethanol, then dried at 110℃ for 5h, calcined at 450℃ for 6h, to prepare catalyst precursor A, Ni is calculated as element The weight of the carrier is 3%, and Mo accounts for 2% of the weight of the carrier based on elements; n-octane: n-hexanol: Tween 80: active component nickel: first auxiliary molybdenum = 0.8:1:0.3:2.4:1, hydrazine hydrate The volume ratio of solution to n-octane is 1:35.

[0033] Activate 20g of catalyst precursor A in a hydrogen-c...

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Abstract

The invention relates to a method for preparing a synthesis gas methanation catalyst. The preparation method of the catalyst firstly prepares a catalyst precursor A; then uses a reducing atmosphere to reduce the catalyst precursor A; and combines the reduced catalyst precursor A with The polyol solution is added to the autoclave for hydrogenation reaction, the reaction effluent is placed and then filtered and dried to obtain the catalyst precursor B; the active component precursor and the second auxiliary agent precursor are dissolved in water to obtain the solution C , and then add the catalyst precursor B, after drying and roasting, the catalyst is obtained. The method of the invention promotes the dispersion of more active components on the carrier surface, not only improves the utilization rate of active metals, but also improves the conversion rate of carbon monoxide and the selectivity of products.

Description

Technical field [0001] The invention relates to a preparation method of a synthesis gas methanation catalyst, in particular to a preparation method of a synthesis gas methanation supported nickel-based catalyst. Background technique [0002] Methanation refers to CO / CO 2 With H 2 Under certain temperature, pressure and catalyst, CH is generated 4 At present, this reaction is widely used in the removal of trace carbon in the synthesis of ammonia or hydrogen, the methanation of coke oven gas, and the production of natural gas from coal. Methanation is an important catalytic technology, especially in the field of fuel applications, which can be used to increase the calorific value of fuel gas and allow the conversion of coke oven gas, coal or biomass to natural gas. In recent years, with the rapid development of my country's coal-based substitute natural gas industry, methanation as one of the core technologies has received more and more attention. [0003] China is a country with "r...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/883B01J29/48B01J23/887C07C9/04C07C1/04
Inventor 任金晨孙晓丹张舒冬张信伟刘继华
Owner CHINA PETROLEUM & CHEM CORP
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