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Amorphous silicon aluminium and preparation method thereof

A technology of amorphous silica-alumina and sodium aluminate, applied in chemical instruments and methods, catalyst activation/preparation, addition of unsaturated hydrocarbons to hydrocarbons, etc., can solve excessive cracking of catalysts, low pore volume and specific surface, pollution Environmental and other issues, to achieve the effect of improving product selectivity, avoiding excessive cracking, and concentrating pore distribution

Active Publication Date: 2011-05-04
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The preparation method is that the alkali metal aluminum salt and silicate form a mixed solution when the pH value is about 12, and then react with aluminum sulfate to prepare a silicon-aluminum carrier. The specific surface of the product is 277m 2 / g, pore volume 0.31ml / g, containing SiO 2 35wt%, the disadvantage is that the pore volume and specific surface are low, as a carrier catalyst, silica-alumina cannot provide higher metal dispersion for active components
[0006] CN1210755A discloses a kind of amorphous silicon aluminum and its preparation method, its alumina content is 10~50wt%, specific surface is 350~600m 2 / g, pore volume 0.8~1.5ml / g, infrared acidity 0.25~0.55mmol / g, its preparation process is NH 4 OH and alumina first form alumina and then decompose silicate, which will produce ammonia and nitrogen-containing wastewater and pollute the environment
In addition, the amorphous silica-alumina strong acid obtained by this method is more, which will cause excessive cracking of the catalyst, which is not conducive to the improvement of catalyst selectivity.
[0007] CN1597093A discloses an amorphous silicon-alumina prepared by carbonization method, containing 8wt%-50wt% of silicon oxide, and the specific surface is 300-550m 2 / g, the pore volume is 0.7-1.5ml / g, and the infrared acidity is 0.32-0.50mmol / g. The disadvantage is that there are many strong acids and relatively few L acids, which will cause excessive cracking of the catalyst, which is not conducive to the improvement of catalyst selectivity.

Method used

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  • Amorphous silicon aluminium and preparation method thereof

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Experimental program
Comparison scheme
Effect test

Embodiment 1

[0028] Prepare solid sodium aluminate to a concentration of 200g Al 2 o 3 / l concentrated sodium aluminate solution, then diluted to a concentration of 20g Al 2 o 3 / L sodium aluminate working solution, take SiO 2 28wt% sodium silicate solution, then diluted to a concentration of 100g SiO2 / l sodium silicate working solution. Take 10L of sodium aluminate working solution and place it in a gel-forming tank, then add 0.3L of sodium silicate working solution, control the reaction temperature at 24°C, and feed CO with a concentration of 55v%. 2 Gas, fed with 80% CO 2 After the gas, while passing CO 2 Add 0.6L of sodium silicate working solution to the gas side, control the pH value of the end of gelation to 10.0, then ventilate and stabilize for 10 minutes, filter the slurry and wash it with 75°C deionized water until neutral. The resulting filter cake was beaten with water at a solid-to-liquid volume ratio of 8:1, treated at 120°C for 2 hours under 1MPa water vapor pressure...

Embodiment 2

[0030] Sodium aluminate working solution concentration 25g Al 2 o 3 / L, sodium silicate working solution concentration 100 SiO 2 / l, take 10L of sodium aluminate working solution and place it in a gel-forming tank, then add 0.5L of sodium silicate working solution, control the reaction temperature at 20°C, and feed CO with a concentration of 35v%. 2 gas, CO 2 When the gas accounts for 50% of the total intake, add 0.6L sodium silicate working solution while ventilating, control the pH value at the end of gelation to 9.5, then ventilate and stabilize for 15 minutes, filter the slurry and wash it with 75°C deionized water to medium The filter cake is beaten with water at a solid-to-liquid volume ratio of 8:1, treated at 120°C and 1.0MPa steam pressure for 2 hours, dried at 120°C for 8 hours, crushed and sieved to obtain the amorphous silicon-alumina product GL-2 .

Embodiment 3

[0032] Sodium aluminate working solution concentration 30g Al 2 o 3 / L, sodium silicate working solution concentration 150 SiO 2 / l, take 10L of sodium aluminate working solution and place it in a gel-forming tank, then add 0.25L of sodium silicate working solution, control the reaction temperature at 30°C, and feed CO with a concentration of 48v%.2 Gas, stop when the pH value reaches 10.0, then ventilate and stabilize for 20 minutes, wash until neutral, add water to the filter cake according to the solid-to-liquid volume ratio of 8:1, and treat it at 130°C for 2 hours under 3MPa steam pressure. After drying at ℃ for 8 hours, crush and sieve to obtain the amorphous silica-alumina product GL-3.

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Abstract

The invention discloses an amorphous silicon aluminium and a preparation method thereof. In the invention, hydro-thermal treatment is carried out on amorphous silicon aluminium obtained by a carbonization method, so that the amorphous silicon aluminium has higher specific surface area and bigger pore volume, the pore distribution is more intensive, and the pore volume the pore diameter of which is 6-10nm accounts for 80-95% of the total pore volume; meanwhile, the acid distribution of the amorphous silicon aluminium is improved; the amount of moderately strong acid and L acid is improved to effectively prevent raw material modules from excessively cracking, which is favourable for improving the selectivity of a target product.

Description

technical field [0001] The invention relates to an amorphous silicon aluminum and a preparation method thereof, in particular to a method for modifying amorphous silicon aluminum prepared by a carbon dioxide neutralization method. Background technique [0002] Amorphous silica-alumina has certain pore structure and specific surface area, so it can be used as catalyst carrier and adsorbent in oil refining and petrochemical industry. Amorphous silica-alumina as a catalyst carrier requires itself to have a large specific surface and pore volume to ensure the dispersion of catalyst active components, and as a carrier for cracking catalysts, amorphous silica-alumina must also have a certain cracking activity (i.e. acidic). [0003] With the rapid development of the petrochemical industry, the demand for amorphous silicon-alumina is increasing, but the amorphous silicon-alumina prepared by the existing technology mostly uses NH 4 OH, which will produce wastewater containing ammo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J32/00B01J21/12B01J37/10B01J35/10C10G11/04C10G47/12C10G49/02C07C2/02
Inventor 孙晓艳樊宏飞王占宇
Owner CHINA PETROLEUM & CHEM CORP
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