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Methanation catalyst for fluidized bed and preparation method of methanation catalyst for fluidized bed

A methanation catalyst, fluidized bed technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problem that the mechanical strength and wear resistance of catalysts need to be improved , the fluidization state is not easy to control, the particle size is not uniform, etc., to achieve the effect of low price, rich porosity, and high catalytic activity

Active Publication Date: 2017-02-15
CHINA NAT OFFSHORE OIL CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Chinese patent CN 104399482 A reports a bimetallic methanation catalyst whose carrier is crushed and calcined iron-containing natural ore and impregnated with Ni. The raw material of the catalyst is cheap and easy to obtain, and has strong wear resistance. The particle size is not uniform, and the fluidized state is not easy to control and unstable
The solution combustion method increases the pores and specific surface area of ​​the catalyst, and promotes the dispersion of active components in the carrier, but the mechanical strength and wear resistance of the prepared catalyst still need to be improved

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0044] Embodiment 1, preparation and application of fluidized bed methanation catalyst

[0045] (1) will contain 260.5g Al(NO 3 ) 3 9H 2 O, 35.5g Zr(NO 3 ) 4 ·5H 2 O and 15.0g Ni(NO 3 ) 2 ·6H 2 Add 2L of the mixed aqueous solution of O into the constant temperature reaction kettle, stir the reaction at a temperature of 80°C, and add Na with a concentration of 10wt% 2 CO 3 aqueous solution, adjust the pH value to 8.0, and react for 1 hour to obtain a reaction precipitate.

[0046] (2) After the precipitate in step (1) is coarsely filtered and washed with deionized water, the pH value is 7.8, and then the silica-alumina composite sol is added, beaten, sprayed, dried at 80°C for 2 hours, and roasted at 600°C for 5 Hours, the carrier particles with an average particle size of 100 μm were produced.

[0047] (3) Preparation containing 135.0g Ni(NO 3 ) 2 ·6H 2 O and 95.5g Mg(NO 3 ) 2 ·6H 2 O 0.5L mixed aqueous solution, impregnate the carrier particles prepared in st...

Embodiment 2

[0052] Embodiment 2, preparation and application of fluidized bed methanation catalyst

[0053] (1) will contain 290.8g Al(NO 3 ) 3 9H 2 O, 30.5g Zr(NO 3 ) 4 ·5H 2 O and 15.0g Ni(NO 3 ) 2 ·6H 2 Add 2.5L of mixed aqueous solution of O into the constant temperature reaction kettle, stir and react at a temperature of 80°C, and add 10% Na 2 CO 3 aqueous solution, adjust the pH value to 8.0, and react for 1 hour to obtain a reaction precipitate.

[0054] (2) After washing the precipitate in step (1) with deionized water, the pH value is 7.8, then adding silica sol, beating, spray molding, drying at 80°C for 2 hours, and roasting at 600°C for 5 hours to obtain an average The particle size is 200 μm carrier particles.

[0055] (3) Preparation containing 125g Ni(NO 3 ) 2 ·6H 2 O and 55.6g Mn(NO 3 ) 2 4H 2 O 0.5L mixed aqueous solution, impregnate the carrier prepared in step (2), impregnate at 50°C for 6h, then put it in an oven at 80°C for 6h, and bake at 400°C for 6...

Embodiment 3

[0060] Embodiment 3, preparation and application of fluidized bed methanation catalyst

[0061] (1) will contain 260.5g Al(NO 3 ) 3 9H 2 O, 40.6g Zr(NO 3 ) 4 ·5H 2 O and 15.0g Ni(NO 3 ) 2 ·6H 2 Add 2.5L of mixed aqueous solution of O into the constant temperature reaction kettle, stir and react at a temperature of 80°C, and add 10% Na 2 CO 3 aqueous solution, adjust the pH value to 8.0, and react for 1 hour to obtain a reaction precipitate.

[0062] (2) After washing the precipitate in step (1) with deionized water, the pH value is 7.8, then adding silica sol, beating, spray molding, drying at 80°C for 2 hours, and roasting at 600°C for 5 hours to obtain an average The particle size is 250 μm carrier particles.

[0063] (3) Preparation containing 140.7g Ni(NO 3 ) 2 ·6H 2 O and 43.6g Ce(NO 3 ) 3 ·6H 2 O 0.5L mixed aqueous solution, impregnate the carrier prepared in step (2), impregnate at 50°C for 6h, then dry it in an oven at 80°C for 6h, and roast at 400°C f...

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Abstract

The invention discloses a methanation catalyst for a fluidized bed and a preparation method of the methanation catalyst for the fluidized bed. The methanation catalyst for the fluidized bed comprises a carrier, an active component and auxiliary agents, and the active component and the auxiliary agents are loaded on the carrier. The carrier is a compound of Al2O3, ZrO2 and NiO or a compound of Al2O3, TiO2 and NiO; the active component is NiO; the auxiliary agents are oxides of at least one of Mg, Ca, La, Ce, Mn, Fe, Cu, Cr and Co. A co-precipitation method is adopted for preparation of the carrier of the catalyst, and uniformity in component distribution is realized; then spray forming is adopted to obtain the micro-spherical catalyst carrier which is high in fluidity and suitable for the fluidized bed. In preparation of the carrier of the catalyst, silicon sol or silicon-aluminum composite sol is added to serve as an adhesive; in a process of quick preparation of the micro-spherical carrier by spray forming, the silicon sol or silicon-aluminum composite sol is dispersed among carrier components, and after high-temperature calcination, the catalyst carrier is high in mechanical strength, abrasion resistance and impact resistance.

Description

technical field [0001] The invention relates to a methanation catalyst used in a fluidized bed and a preparation method thereof, belonging to the technical field of methanation catalysts. Background technique [0002] As a clean, environmentally friendly, and efficient energy source, natural gas accounts for an increasing proportion in my country's energy structure year by year. The contradiction between supply and demand has become increasingly prominent, and the degree of dependence on foreign countries has increased. my country is a "coal-rich, oil-poor, and gas-poor" country. The use of coal to synthesize natural gas and coke oven gas to synthesize natural gas is of great significance to optimize my country's energy structure, save energy and reduce emissions, and reduce environmental pollution. [0003] Methanation technology is the key technology for coal-to-synthetic natural gas and coke-oven gas-to-synthetic natural gas. The methanation reaction is a highly exotherm...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/755B01J23/83B01J23/889C07C1/04C07C9/04C10L3/08
CPCB01J23/002B01J23/78B01J23/83B01J23/8892B01J2523/00C07C1/0435C07C9/04C10L3/08B01J2523/31B01J2523/22B01J2523/41B01J2523/847B01J2523/48B01J2523/72B01J2523/3712B01J2523/47
Inventor 张瑜宋鹏飞穆祥宇王秀林张勃高振姚辉超侯海龙
Owner CHINA NAT OFFSHORE OIL CORP
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