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Preparation method of bulk phase hydrocracking catalyst

A cracking catalyst and catalyst technology, applied in the direction of catalyst activation/preparation, physical/chemical process catalyst, heterogeneous catalyst chemical elements, etc., can solve the problems of high investment cost, long production process, complicated operation, etc., and reduce operation cost, large economic benefits, and the effect of increasing the added value of products

Pending Publication Date: 2022-05-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The properties such as the pour point and aromatics content of the diesel fraction produced by the catalyst prepared by hydrocracking cannot meet the standard requirements of industrial-grade white oil, and can only be used as industrial-grade white oil base oil, and must undergo deep dewaxing and hydrofining. Industrial-grade white oil products can only be obtained after technical treatment. The production process is long, the operation is complicated and the investment cost is high.

Method used

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  • Preparation method of bulk phase hydrocracking catalyst
  • Preparation method of bulk phase hydrocracking catalyst
  • Preparation method of bulk phase hydrocracking catalyst

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] (1) Mix the mixed solution containing nickel chloride and aluminum chloride (the mass concentration of Ni is 28g / L in terms of NiO, and the mass concentration of Al in terms of Al 2 o 3 The mass concentration is 9g / L), 12wt% sodium hydroxide solution and sodium tungstate solution (W is expressed as WO 3 The mass concentration is 42g / L) and flowed into the gelation tank with a certain amount of bottom water for gelation reaction. The gelation temperature is 60°C, the pH value is 7.8, and the gelation time is 60 minutes. After the gelation is completed, precipitation is obtained. material slurry;

[0038] (2) Mix the slurry containing β molecular sieve (15.2 grams of molecular sieve, solid-to-liquid volume ratio of 1:3.) and the sediment slurry from step (1), and then age it. The aging temperature is 75°C, and the aging pH value is 8.0. Aged for 2 hours. After aging, add molybdenum oxide, beat and mix, filter the obtained slurry, dry the filter cake at 80°C for 10 hour...

Embodiment 2

[0041] (1) The mixed solution containing nickel chloride and aluminum chloride (the mass concentration of Ni as NiO is 36g / L, Al as Al 2 o 3 The mass concentration is 10g / L), 15wt% sodium hydroxide solution and sodium tungstate solution (W is expressed as WO 3 The mass concentration of the meter is 42g / L) and flow into the gelation tank with a certain amount of bottom water for gelation reaction. The gelation temperature is 55°C, the pH value is 7.8, and the gelation time is 48 minutes. After the gelation is completed, you can get sediment slurry;

[0042] (2) Mix the β molecular sieve-containing slurry (solid-to-liquid volume ratio 1:4) with the sediment slurry from step (1), and then age it. The aging temperature is 70°C, the aging pH value is 8.0, and the aging time is 2.2 hours. After aging, molybdenum oxide is added, beaten and mixed, the obtained slurry is filtered, the filter cake is dried at 85°C for 16 hours, rolled, and extruded to obtain a molded product;

[0043...

Embodiment 3

[0045] (1) In the mixed solution containing nickel sulfate and aluminum chloride (the mass concentration of Ni is 32g / L as NiO, Al is 32g / L as Al 2 o 3 The mass concentration of meter is 7g / L), 10wt% sodium hydroxide solution, sodium tungstate solution (W is expressed as WO 3 The mass concentration of the meter is 46g / L) and flow into the gelation tank with a certain amount of bottom water for gelation reaction. The gelation temperature is 65°C, the pH value is 7.6, and the gelation time is 84 minutes. After the gelation is completed, you can get sediment slurry;

[0046] (2) Mix the slurry containing β-molecular sieve (solid-to-liquid volume ratio: 1:2.5) and the sediment slurry from step (1), and then age, the aging temperature is 76°C, the aging pH value is 8.3, and after aging for 3.5 hours, Then, the sediment slurry was further aged under high pressure, the pressure was 12.5 MPa, the aging temperature was 140° C., the aging time was 1.5 hours, and the pH value was 11.5....

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Abstract

The invention discloses a preparation method of a bulk phase hydrocracking catalyst. The preparation method comprises the following steps: (1) preparing slurry containing nickel, tungsten and aluminum precipitates: carrying out a parallel flow gel-forming reaction on a mixed solution containing Ni and Al, a sodium tungstate solution and a precipitator; (2) preparing a forming substance: mixing beta molecular sieve slurry with the precipitate slurry obtained in the step (1), then aging, adding MoO3 into the aged material, pulping and mixing, and carrying out solid-liquid separation, drying and forming; and (3) desalting the molded substance, namely soaking the molded substance in an organic acid solution of a carboxylic acid polymer and / or an organic phosphonic acid compound, curing the soaked molded substance, washing to remove salt separated out to the surface of the molded substance, drying and roasting to obtain the hydrocracking catalyst. The catalyst prepared by the method has high isomerization and aromatic hydrocarbon conversion capacities, and is suitable for a hydrocracking process for producing high value-added special oil.

Description

technical field [0001] The invention belongs to the technical field of petroleum refining, and in particular relates to a preparation method of a bulk hydrocracking catalyst. Background technique [0002] Special oils are widely used in food, medicine, daily chemicals, clothing, paint, metallurgical manufacturing, automobile production and many other industries. Compared with conventional hydrocracking products such as refined oil and chemical raw materials, the quality indicators of special oil products are significantly different. For example, transformer oil and industrial white oil have very strict indicators in terms of low-temperature fluidity and aromatics content. According to the different grades of industrial white oil, the pour point index is -3~-9°C, and the mass percentage of aromatic hydrocarbons is required to be no more than 5%. Transformer oil depends on the lowest cold-state operation temperature in actual application, the product pour point index ranges f...

Claims

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Application Information

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IPC IPC(8): B01J29/78B01J35/10B01J37/03B01J37/00B01J37/08C10G45/54C10G45/64
CPCB01J29/7815B01J23/002B01J37/031B01J37/0009B01J37/0018B01J37/088C10G45/54C10G45/64B01J2523/00C10G2300/302C10G2300/308B01J35/30B01J35/615B01J35/633B01J35/647B01J2523/31B01J2523/68B01J2523/69B01J2523/847Y02P20/52
Inventor 徐学军王海涛李娟王继锋
Owner CHINA PETROLEUM & CHEM CORP