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Hydrocarbon conversion catalyst containing MFI zeolite and preparation method thereof

A catalyst and zeolite technology, applied in physical/chemical process catalysts, hydrocarbon cracking to hydrocarbons, molecular sieve catalysts, etc., can solve the problems of improving performance of molecular sieve catalysts containing MFI structure, not involving anti-metal pollution, reducing coke yield, etc. , to achieve good activity stability and selectivity, good anti-iron pollution ability, and increase yield

Pending Publication Date: 2022-05-03
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

This method does not involve how to make the molecular sieve with MFI structure have a good conversion effect in the case of metal pollution, and does not involve the problem of reducing the coke yield
[0009] The above prior art does not disclose how to further improve the performance of molecular sieve catalysts containing MFI structure when used in heavy oil conversion, and does not involve the problem of anti-metal pollution

Method used

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  • Hydrocarbon conversion catalyst containing MFI zeolite and preparation method thereof
  • Hydrocarbon conversion catalyst containing MFI zeolite and preparation method thereof
  • Hydrocarbon conversion catalyst containing MFI zeolite and preparation method thereof

Examples

Experimental program
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Embodiment approach

[0038] According to the first specific embodiment of the hydrocarbon conversion catalyst containing MFI structure zeolite provided by the present invention, wherein the high specific heat capacity matrix material contains Al 2 o 3 5-94.5% by weight of alumina, MnO 2 5-94.5% by weight manganese oxide and P 2 o 5 0.5-10% by weight phosphorus oxide, boron nitride-free. For example, the high specific heat capacity matrix material includes 15-70% by weight or 20-65% by weight or 25-60% by weight of manganese oxide, 29-84% by weight or 35-80% by weight or 39-74% by weight of oxide Aluminum and 0.8-8% by weight phosphorus oxide.

[0039] According to the first specific embodiment of the hydrocarbon conversion catalyst containing MFI structure zeolite provided by the present invention, the pore volume of the high specific heat capacity matrix material is 0.5-1.0 cm 3 / g such as 0.55-0.8cm 3 / g. The average pore diameter of the high specific heat capacity matrix material is 3-12...

specific Embodiment approach

[0047] A specific embodiment, the preparation method of the high specific heat capacity matrix material, comprises the following steps:

[0048] (1) The aluminum source solution and the alkali solution are mixed to form a gel at room temperature to 85° C., and the pH value of the formed colloid is controlled to be 7-11;

[0049] (2) configuration pH is the manganese salt solution that is 3-7, manganese salt solution is mixed with urea, stirs; Urea and manganese ion molar ratio are 1-5; The temperature that this manganese salt solution mixes with urea has no special requirement, for example Carry out the mixing at room temperature, the stirring time is for example 30-60 minutes;

[0050] (3) Mix the product obtained in step (1), the product obtained in step (2) and optional boron nitride, and age at room temperature to 120° C. for 4-72 hours; and

[0051] (4) Filtrate the aged product obtained in step (3), optionally perform a first wash to obtain an aged solid precipitate, co...

preparation example 1

[0149]This example illustrates the preparation process of the high specific heat capacity matrix material provided by the present invention.

[0150] The concentration of 350gAl 2 o 3 / L Al 2 (SO 4 ) 3 solution with CO 3 2- The ammonium carbonate solution with a concentration of 0.10 mol / L was mixed at 20° C. to form a colloid, and the obtained colloid had a pH value of 7.5, and a slurry A was obtained. To a concentration of 145gMnO 2 / L MnCl 2 Add hydrochloric acid (concentration 36% by weight) to the solution to control the pH=3.5, then add urea to the solution, the molar ratio of urea to manganese ions is 2, and stir at room temperature for 30 minutes to obtain solution B. Add solution B to slurry A, stir and age at 80°C for 24 hours, wait until the temperature of the system drops to room temperature, filter, and rinse with deionized water until the rinsed water is neutral, and an aged solid precipitate is obtained, and then According to the aged solid precipitate ...

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Abstract

The invention belongs to the technical field of molecular sieve catalyst preparation, and relates to an MFI zeolite-containing hydrocarbon conversion catalyst and a preparation method thereof, the catalyst contains zeolite comprising MFI structure zeolite, a phosphorus-containing matrix material and a heat-resistant inorganic oxide; the phosphorus-containing matrix material contains the following components in percentage by weight: 5-94.5% of aluminum oxide, 5-94.5% of manganese oxide and 0.5-10% of phosphorus oxide, and the specific heat capacity is 1.3-2.0 J / (g.K). The preparation method comprises the following steps: forming slurry from the phosphorus-containing matrix material, the zeolite, the heat-resistant inorganic oxide binder, the optional clay and the optional auxiliary compound, and carrying out spray drying. The catalyst is good in metal pollution resistance and wear resistance, is used for heavy oil conversion, and has relatively high heavy oil conversion capacity and high light olefin yield, and unexpectedly, the light aromatic hydrocarbon yield is relatively high.

Description

technical field [0001] The invention belongs to the technical field of preparation of molecular sieve catalysts, and relates to a hydrocarbon conversion catalyst containing molecular sieves with an MFI structure and a preparation method thereof. Background technique [0002] Molecular sieves are widely used in the conversion process of hydrocarbons. Different molecular sieves usually play different roles in the conversion process. Different target products can be obtained when used under different hydrocarbon conversion conditions. Co-actions can also have different transformation properties. Molecular sieves with MFI structure such as ZSM-5 molecular sieves can be used in hydrocarbon oil conversion to produce light olefins such as ethylene and propylene. [0003] The heavy oil catalytic cracking reaction that produces more light olefins is usually carried out at a higher temperature than the catalytic cracking reaction. This is because for the conventional catalytic cracki...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/187B01J27/24B01J35/10B01J29/48B01J29/80C10G11/05C07C4/06C07C11/04C07C11/06C07C15/04C07C15/06C07C15/08C04B38/00C04B35/10C04B35/622
CPCB01J27/187B01J27/24B01J29/80B01J29/48C10G11/05C07C4/06C04B38/00C04B35/10C04B35/622B01J29/166B01J2229/20C04B2235/3267C04B2235/34C04B2235/386B01J35/615B01J35/638B01J35/635B01J35/647C07C11/04C07C11/06C07C15/04C07C15/06C07C15/08C04B38/0054B01J21/04B01J23/34B01J27/14B01J29/18B01J29/08B01J29/40C10G11/02Y02P20/52
Inventor 刘倩倩陈振宇林伟杨雪宋海涛
Owner CHINA PETROLEUM & CHEM CORP