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Catalytic cracking aid, preparation method and application thereof, and hydrocarbon oil catalytic cracking method

A technology of catalytic cracking additives and adhesives, applied in catalytic cracking, molecular sieve catalysts, chemical instruments and methods, etc., can solve the problems of low propylene selectivity and limited propylene growth rate, and achieve simple operation, easy control of conditions, The effect of simple process

Active Publication Date: 2021-02-23
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Such as the catalytic cracking catalysts or additives provided by the above-mentioned patent documents, because they only pay attention to the modification of conventional ZSM-5 molecular sieves, they do not pay attention to the role of the carrier, and ignore the secondary conversion of cracked products in the cracking reaction process. Although they can effectively Increase the yield of low-carbon olefins and increase the octane number of catalytic cracking gasoline, but the selectivity for propylene is not high in the catalytic cracking reaction process, and the increase of propylene concentration in liquefied gas is limited

Method used

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  • Catalytic cracking aid, preparation method and application thereof, and hydrocarbon oil catalytic cracking method
  • Catalytic cracking aid, preparation method and application thereof, and hydrocarbon oil catalytic cracking method
  • Catalytic cracking aid, preparation method and application thereof, and hydrocarbon oil catalytic cracking method

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Embodiment approach

[0023] According to the present invention, the binder can be selected with reference to the prior art, but according to a preferred embodiment, the binder includes the first binder and the second binder, that is, the preparation of the auxiliary agent The binder includes the first binder and the second binder; wherein, the first binder is at least one of kaolin, alumina, silicon oxide and diatomaceous earth, and the second binder is The mixture is acidic silica sol and / or acidic aluminum sol, and the mass ratio of the first binder to the second binder is 1:(0.5-2.0). In the present invention, the binder in the catalytic cracking additive is described in terms of its source, in order to better explain the present invention. It should be understood that the sol exists in the form of oxides in the catalytic cracking aid.

[0024] According to the present invention, the modifying agent can cover and neutralize the acid centers on the surface of the catalytic cracking aid, and at ...

Embodiment 1

[0067] 1) Preparation of one-dimensional through-channel mesoporous silica material

[0068] Add 20g of P123 and 30g of N,N-dimethylformamide into 600g of 1M hydrochloric acid, stir at 40°C until P123 is completely dissolved, then add 40g of methyl orthosilicate to the above solution dropwise, and stir at 40°C After 15 hours, the solution was transferred to a polytetrafluoroethylene-lined reactor and crystallized at 60°C for 24 hours. After the hydrothermal reaction, the solid product was separated from the mother liquor by filtration, washed with deionized water until neutral, and dried in air at 110° C. for 5 hours to obtain the raw powder of mesoporous silica material. Mix 20g of mesoporous silica material raw powder with 200g of tetrahydrofuran, reflux extraction at 70°C for 24h, then filter, wash, and vacuum dry at 60°C for 5h to obtain a one-dimensional through-channel mesoporous silica material. The pore structure parameters of the mesoporous silica material: the pore ...

Embodiment 2

[0074] 1) Preparation of one-dimensional through-channel mesoporous silica material

[0075] Add 20g of P123 and 60g of N,N-dimethylformamide into 1000g of 1M hydrochloric acid, stir at 25°C until P123 is completely dissolved, then add 60g of methyl orthosilicate to the above solution dropwise, and stir at 25°C After 30 hours, the solution was transferred to a polytetrafluoroethylene-lined reactor and crystallized at 50°C for 40 hours. After the hydrothermal reaction, the solid product was separated from the mother liquor by filtration, washed with deionized water until neutral, and dried in air at 70°C for 10 hours to obtain the raw powder of mesoporous silica material. Mix 20g of mesoporous silica material raw powder with 200mL of acidified methanol (the volume ratio of methanol to concentrated hydrochloric acid is 20:1), reflux extraction at 90°C for 12h, then filter, wash, and vacuum-dry at 60°C for 5h to obtain a Mesoporous silica materials with straight-through channels...

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Abstract

The invention relates to the field of hydrocarbon oil catalytic conversion, and discloses a catalytic cracking aid, a preparation method and application thereof, and a hydrocarbon oil catalytic cracking method. The catalytic cracking aid comprises high-silicon zeolite, mesoporous silica, an adhesive and a modifier; wherein the high-silicon zeolite is hydrogen type zeolite with an MFI skeleton structure, and the molar ratio of silicon to aluminum (SiO2 / Al2O3) is not less than 100; the mesoporous silica is a one-dimensional straight-through pore channel mesoporous silica material; the modifier is selected from at least one of alkaline earth metal oxide, rare earth metal oxide and nonmetal oxide. The catalytic cracking aid is used in the catalytic cracking process of hydrocarbon oil, and canimprove the concentration of propylene in liquefied gas and further improve the octane number of catalytically cracked gasoline under the condition of ensuring the yield of catalytically cracked liquefied gas.

Description

technical field [0001] The invention relates to the field of catalytic conversion of hydrocarbon oil, in particular to a catalytic cracking additive, a preparation method and application thereof, and a method for catalytic cracking of hydrocarbon oil. Background technique [0002] Propylene is an important chemical basic raw material next to ethylene, mainly used in the production of polypropylene, acrylonitrile, propylene oxide, acrylic acid, cumene and other chemicals. my country's propylene industry still maintains a medium-speed growth. It is estimated that by 2020, propylene production capacity, production, imports, apparent consumption and equivalent demand will reach about 39.5 million tons / year, 33.5 million tons, 1.2 million tons, 34.7 million tons and 37 million tons respectively. Equivalent demand and production There is still a gap of 3.5 million tons. From the perspective of the supply and demand of propylene in my country, on the one hand, there is a shortage...

Claims

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Application Information

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IPC IPC(8): B01J29/40C10G11/05
CPCB01J29/405C10G11/05C10G2300/1037C10G2300/107C10G2300/1077Y02P20/52
Inventor 王定博亢宇刘红梅
Owner CHINA PETROLEUM & CHEM CORP
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