Hydrocracking catalyst carrier, hydrocracking catalyst and preparation methods of hydrocracking catalyst carrier and hydrocracking catalyst

A catalyst carrier and hydrocracking technology, applied in the direction of catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of unsatisfactory industrial requirements, high isomerization content of tail oil, and unsatisfactory product yield and other problems, to achieve the effect of good hydrogenation function, excellent product quality, and improved catalyst activity and selectivity

Active Publication Date: 2022-05-10
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] CN105582992A discloses a hydroisomerization catalyst, its preparation method and application, and a method for hydroisomerization of hydrocracking tail oil. This technology can use wax oil as raw material oil and prepare it by using isomer-containing molecular sieves The hydrocracking catalyst produced high-quality products. The tail oil has high isomer content, low freezing point and high viscosity index. It is the raw material of high-quality lubricating oil base oil. However, the catalyst uses a precious metal catalyst, which limits the application in industry.
This kind of technology can produce various high-quality hydrocracking products by using wax oil as raw material oil, and using the hydrocracking method containing Y-type molecular sieve catalyst and isomeric type molecular sieve hydrocracking catalyst at the same time, but the product yield is not ideal
[0007] CN101450320B discloses a hydrocracking catalyst containing Y molecular sieve and its preparation method. In this invention, the Y molecular sieve is first formulated with aluminum salt and acid into a mixed solution, and then the hydrothermally treated Y molecular sieve is treated with the above mixed solution , the catalyst is finally prepared, although the catalyst has high activity, but its nitrogen tolerance is poor, and its industrial use is limited
The nitrogen resistance of the catalyst prepared by using the carrier is improved, but the activity of the catalyst is poor and cannot meet the industrial requirements

Method used

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  • Hydrocracking catalyst carrier, hydrocracking catalyst and preparation methods of hydrocracking catalyst carrier and hydrocracking catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0078] (1) Preparation of Beta / Al-SBA-15 Composite Molecular Sieve

[0079] (1) Preparation of amorphous silica-alumina dry rubber powder A1 and slurry: sodium aluminate solution concentration 18gAl 2 o 3 / L, the concentration of sodium silicate solution is 80SiO 2 / L, take 0.30L sodium aluminate solution and put it into the gel-forming tank, then add 0.30L sodium silicate 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 65% of the total intake, add 0.30L sodium silicate solution while ventilating to control the pH value of the gel to 9.2, then ventilate and stabilize for 20 minutes, filter the slurry and wash it with 65°C deionized water until neutral. The filter cake was beaten with water at a solid-to-liquid volume ratio of 10:1, treated at 130°C and 3.5 MPa steam pressure for 3 hours, dried at 120°C for 6 hours, crushed and sieved to obtain the amorphous silica-alumina product A1. The pr...

Embodiment 2

[0088] (1) Preparation of Beta / Al-SBA-15 Composite Molecular Sieve

[0089] (1) Preparation of amorphous silica-alumina dry rubber powder A2 and slurry: concentration of sodium aluminate solution 32gAl 2 o 3 / L, the concentration of sodium silicate solution is 115gSiO 2 / L, take 0.8L sodium aluminate solution and put it into a gel-forming tank, then add 0.2L sodium silicate solution, control the reaction temperature at 22°C, and feed CO with a concentration of 48v%. 2 gas, CO 2 When the gas accounts for 55% of the total feed volume, add 0.25L sodium silicate solution while ventilating to control the pH value of the gel to 9.8, then ventilate and stabilize for 20 minutes, filter the slurry and wash it with 75°C deionized water until neutral. The filter cake was beaten with water at a solid-to-liquid volume ratio of 8:1, treated at 110°C and 3.0 MPa steam pressure for 3 hours, dried at 120°C for 8 hours, crushed and sieved to obtain amorphous silicon-aluminum product A2, amor...

Embodiment 3

[0098] (1) Preparation of Beta / Al-SBA-15 Composite Molecular Sieve

[0099] (1) Preparation of amorphous silica-alumina dry rubber powder A3 and slurry: sodium aluminate solution concentration 20gAl 2o 3 / L, sodium silicate working solution concentration 85gSiO 2 / L, take 1.08L of sodium aluminate solution and place it in a gel-forming tank, then add 0.2L of sodium silicate solution, control the reaction temperature at 32°C, and feed CO with a concentration of 55v%. 2 Gas, stop when the pH value reaches 9.8, then ventilate and stabilize for 20 minutes, wash until neutral, add water to the filter cake according to the solid-liquid volume ratio of 8:1, and treat it at 130°C for 2.5 hours under 3.9MPa steam pressure. After drying at 120°C for 8 hours, it was crushed and sieved to obtain the amorphous silica-alumina product A3. The properties of amorphous silica-alumina dry rubber powder A3 are shown in Table 1. The prepared amorphous silica-alumina A3 and deionized water were...

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Abstract

The invention discloses a hydrocracking catalyst carrier, a hydrocracking catalyst and a preparation method thereof. The hydrocracking catalyst carrier comprises a Beta / Al-SBA-15 composite molecular sieve, amorphous silica-alumina I and alumina, the acid content of medium and strong acids in the Beta / Al-SBA-15 composite molecular sieve is 0.6-1.2 mL / g, and the ratio of the acid B to the acid L is less than 0.80. The hydrocracking catalyst prepared by adopting the hydrocracking catalyst carrier has excellent comprehensive performance, is especially used in the hydrocracking reaction process of shale oil with a complex raw material structure, and has excellent product quality.

Description

technical field [0001] The invention relates to a hydrocracking catalyst carrier, a hydrocracking catalyst and a preparation method thereof. The catalyst is particularly suitable for the hydrocracking process of shale oil distillate oil. Background technique [0002] Among natural resources, oil shale, like petroleum, is mainly produced by algae and other lower plankton through decay and coalification. The shale oil "squeezed" from oil shale through low carbonization and other methods is called "artificial petroleum". After further processing and refining, liquid fuels such as gasoline, kerosene, and diesel can be produced. In the initial stage of oil shale mining, the development of this industry was restricted due to the unqualified technology and the pollution of the environment during the production process. In recent years, with the advancement of technology, this problem has been well solved. It is foreseeable that under the current situation of shortage of oil resou...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/80B01J35/10B01J37/02C10G47/20
CPCB01J29/80B01J37/0203B01J35/1019B01J35/1038B01J35/1042B01J35/1061C10G47/20B01J29/7815B01J29/0341B01J2229/186C10G2300/307C10G2400/04C10G2300/70Y02P20/52
Inventor 唐兆吉杜艳泽刘建锟樊宏飞
Owner CHINA PETROLEUM & CHEM CORP
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