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Hydrocracking catalyst carrier, hydrocracking catalyst and preparation method and application thereof

A catalyst carrier and hydrocracking technology, which is applied in the direction of catalyst carrier, physical/chemical process catalyst, molecular sieve catalyst, etc., can solve the problems of poor catalyst activity, inability to meet industrial requirements, use restrictions, etc., and achieve acidity and pore structure improvement, Favorable effects of diffusion spillover and selective promotion of ring opening

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 prepared into a mixed solution with aluminum salt and acid, and then the Y molecular sieve is treated with the above mixed solution after hydrothermal treatment. , 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 method and application thereof

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Experimental program
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Effect test

Embodiment 1

[0079] (1) Preparation of hydrocracking catalyst carrier precursor

[0080] (1) Preparation of amorphous silica-alumina dry glue A1 and slurry: sodium aluminate solution concentration 20gAl 2 o 3 / L, the concentration of sodium silicate solution is 100gSiO 2 / L, take 0.25L of sodium aluminate solution and put it into a gel-forming tank, then add 0.35L of sodium silicate solution, control the reaction temperature at 20°C, and feed CO with a concentration of 40v%. 2 gas, CO 2 When the gas accounts for 50% of the total intake, add 0.50L sodium silicate solution while ventilating to control the pH value of the gel to 9.5, 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 under 3.5MPa water vapor pressure for 2 hours, dried at 120°C for 6 hours, crushed and sieved to obtain the amorphous silica-alumina product A1. Th...

Embodiment 2

[0089] (1) Preparation of hydrocracking catalyst carrier precursor

[0090] (1) Preparation of amorphous silica-alumina dry glue A2 and slurry: sodium aluminate solution concentration 25gAl 2 o 3 / L, the concentration of sodium silicate solution is 50gSiO 2 / L, put 0.4L sodium aluminate solution into the gel-forming tank, then add 0.6L sodium silicate solution, control the reaction temperature at 22°C, and feed CO with a concentration of 35v%. 2 Gas, when CO2 gas is introduced to account for 50% of the total amount, add 0.2L sodium silicate solution while ventilating, control the pH value of the gel to be 9.5, then ventilate and stabilize for 20 minutes, filter the slurry and wash it with 75°C deionized water Wash until neutral, add water to the filter cake at a solid-to-liquid volume ratio of 8:1 and beat, treat at 120°C for 2 hours under 3.0MPa water vapor pressure, dry at 120°C for 8 hours, crush and sieve to obtain amorphous silicon-alumina products A2, the properties o...

Embodiment 3

[0099] (1) Preparation of hydrocracking catalyst carrier precursor

[0100] (1) Preparation of amorphous silica-alumina dry glue A3 and slurry: sodium aluminate solution concentration 20gAl 2 o 3 / L, sodium silicate working solution concentration 75gSiO 2 / L, take 1.25L sodium aluminate solution and place it in a gel-forming tank, then add 0.5L sodium silicate solution, control the reaction temperature at 32°C, and feed CO with a concentration of 52v%. 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 9:1, and treat it at 130°C for 3 hours under 3.9MPa water vapor pressure. After drying at 130°C for 8 hours, it was crushed and sieved to obtain the amorphous silica-alumina product A3. The properties of the amorphous silica-alumina dry adhesive A3 are shown in Table 1. The prepared amorphous silica-alumina A3 and deionized water are mixed and b...

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Abstract

The invention discloses a hydrocracking catalyst carrier, a hydrocracking catalyst and a preparation method and application thereof. The carrier comprises an Al-SBA-15 mesoporous molecular sieve, a beta molecular sieve, aluminum oxide and nano silicon dioxide, and the pore distribution of the Al-SBA-15 mesoporous molecular sieve comprises: the pore diameter lt; the pore volume of 4 nm pores accounts for 20% or less of the total pore volume, preferably 15% or less; in the Al-SBA-15 mesoporous molecular sieve, the ratio of acid B to acid L is 1 or below. 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 and application 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 short...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/80B01J32/00B01J21/08B01J35/10C10G47/20
CPCB01J29/80B01J21/08C10G47/20B01J29/7815B01J29/0341C10G2300/307C10G2400/04B01J2229/186C10G2300/70B01J35/394B01J35/615B01J35/633Y02P20/52
Inventor 杜艳泽唐兆吉樊宏飞
Owner CHINA PETROLEUM & CHEM CORP
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