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Hydrocracking catalyst containing amorphous aluminum silicide and preparation thereof

An amorphous silica-alumina, hydrocracking technology, applied in metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, molecular sieve catalysts, etc., can solve the problem of low specific surface and pore volume of amorphous silica-alumina , pore volume, low specific surface area, non-concentrated pore distribution, etc., to achieve the effect of large space and specific surface carrying metal, increasing effective components, and improving the uniformity of distribution

Active Publication Date: 2008-08-13
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The specific surface and pore volume of the amorphous silica-alumina are low, which cannot provide higher metal dispersion for active components, and the acidity is also low, so it is not suitable for use as a carrier for cracking catalysts
[0008] CN 1597093A introduces a kind of amorphous silicon aluminum prepared by carbonization method, intermittent production operation, SiO 2 The content is 8% to 50%, but the pore volume and specific surface area are relatively low, and the pore distribution is not concentrated, which needs further improvement

Method used

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  • Hydrocracking catalyst containing amorphous aluminum silicide and preparation thereof

Examples

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Effect test

example 1

[0034] Prepare 700 solid sodium aluminate to a concentration of 200g Al 2 O 3 / l concentrated sodium aluminate solution, and then diluted to a concentration of 35gAl 2 O 3 / L Sodium aluminate working solution (a), which contains SiO 2 28wt% sodium silicate solution, then diluted to a concentration of 150gSiO 2 / l Sodium silicate working solution 2L (b). Take a 30L steel to make a rubber tank, and open the valves of the containers (a) and (b) respectively, and at the same time ventilate and pass in CO with a concentration of 45v% 2 Gas, set the flow rate of (a) and (b) so that the reaction time is 1 hour, and quickly adjust CO 2 The pH of the system is maintained at about 10.0, and the reaction temperature is 30°C. After the reaction of (a) and (b) is completed, stop the introduction of CO 2 , Then ventilate and stabilize for 40 minutes, filter the slurry and wash with 85°C deionized water until it is neutral. It was dried at 120°C for 8 hours, crushed and sieved to obtain amorphou...

example 2

[0036] Formulated 800 solid sodium aluminate to a concentration of 200g Al 2 O 3 / l concentrated sodium aluminate solution, and then diluted to a concentration of 40gAl 2 O 3 / L Sodium aluminate working solution (a), which contains SiO 2 28wt% sodium silicate solution, and then diluted to a concentration of 200gSiO 2 / l Sodium silicate working solution 1L (b). Take a 30L steel to make a rubber tank, and open the valves of the containers (a) and (b) respectively, and at the same time ventilate and inject CO with a concentration of 50v% 2 Gas, set the flow rate of (a) and (b) so that the reaction time is 50 minutes, and quickly adjust the CO 2 The pH of the system is maintained at about 10.5, and the reaction temperature is 35°C. After the reaction of (a) and (b) is completed, stop the introduction of CO 2 , Then ventilate and stabilize for 40 minutes, filter the slurry and wash with 80℃ deionized water to neutrality. It was dried at 120°C for 8 hours, crushed and sieved to obtain a...

example 3

[0038] Prepare 600 solid sodium aluminate to a concentration of 200g Al 2 O 3 / l concentrated sodium aluminate solution, and then diluted to a concentration of 30gAl 2 O 3 / L Sodium aluminate working solution (a), which contains SiO 2 28wt% sodium silicate solution, then diluted to a concentration of 100gSiO 2 / l Sodium silicate working solution 4L (b). Take a 30L steel to make a rubber tank, and open the valves of the containers (a) and (b) respectively, and at the same time ventilate and inject CO with a concentration of 50v% 2 Gas, set the flow rate of (a) and (b) so that the reaction time is 70 minutes, and quickly adjust the CO 2 The pH of the system is maintained at about 9.5, and the reaction temperature is 40°C. After the reaction of (a) and (b), stop the introduction of CO 2 , Then ventilate and stabilize for 1 hour, filter the slurry and wash with 85°C deionized water until it is neutral. It was dried at 120°C for 8 hours, crushed and sieved to obtain amorphous silicon-a...

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Abstract

The present invention provides a hydrocracking catalyst containing amorphous silica-alumina and preparing method. The amorphous silica-alumina in the catalyst employs parallel current coexisting method, not only has a simple process, easily controlling, but also employs CO2 and wind mixing, the reactant is adequately mixed, silica and alumina are effectively mutual action, a large specific surface area and a large specific pore volume are formed, pore distribution is very concentrative, 4-10nm pore volume is about 85%-95% of the total pore volume, pore volume which aperture is bigger than 15nm, is below 5% of the total pore volume. The amorphous silica-alumina provides enough channel to the reactant, benefits for enter and exit of reactant and resultant, greatly enhances effectively element of carrier, enhances the homogeneity of the acid center distributing on the channel, in addition, the invention provides larger space and specific surface to carry metal, the hydrogenation metal has high dispersivity, the catalyst not only has feasible schizolysis activity, but also bas high hydrogenation activity and medium oil selectivity.

Description

Technical field [0001] The invention relates to a hydrocracking catalyst and a preparation method thereof, in particular to a hydrocracking catalyst containing amorphous silicon and aluminum for processing heavy hydrocarbon raw materials and producing middle distillate oil. Background technique [0002] Since the beginning of the 21st century, the crude oil processed by the world's refineries has become heavier, the sulfur and heavy metal content in crude oil has risen significantly, and the environmental protection regulations of various governments have become increasingly stringent. Clean production processes must be adopted to make the most effective use of petroleum resources, reduce material consumption, energy consumption and pollutant emissions in the production process, and produce environmentally friendly petroleum products. As a clean production process for deep processing of heavy oil, hydrocracking meets the requirements of sustainable development. Therefore, the hyd...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/85B01J29/80B01J29/08C10G47/20
Inventor 孙晓艳樊宏飞王战宇
Owner CHINA PETROLEUM & CHEM CORP
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