Multifunctional catalysis composition

A composition and oxide technology, applied in the field of multifunctional catalytic compositions, can solve the problem of high gasification temperature

Active Publication Date: 2014-02-12
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] The technical problem to be solved by the present invention is to provide a catalytic composition suitable for cracking conversion of petroleum hyd

Method used

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Experimental program
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preparation example Construction

[0045] In the preparation process of the mesoporous silicon-aluminum material of the present invention, the aluminum source can be various aluminum sources conventionally used in the preparation process of the mesoporous silicon-aluminum material, for example, it can be selected from aluminum nitrate, aluminum sulfate or aluminum chloride. one or more of .

[0046] In the preparation process of the mesoporous silica-alumina material of the present invention, the silicon source can be various silica-alumina conventionally used in the preparation process of the mesoporous silica-alumina material, such as silica gel, water glass, sodium silicate, tetraethyl At least one of silicon, silicon oxide, silica sol and silica gel.

[0047] In the preparation process of the mesoporous silica-alumina material of the present invention, the alkaline solution can be various conventional alkaline solutions, for example, it can be one of ammonia water, potassium hydroxide solution, sodium metaa...

Embodiment approach

[0053] The preparation method of described catalytic composition provided by the present invention, a kind of preferred embodiment, comprises the following steps:

[0054] (1) Mix and beat the non-ion-exchanged mesoporous silica-alumina material with water to obtain a slurry, and then contact the obtained slurry with an inorganic acid at room temperature to 100°C for at least 0.2 hours to obtain a sodium oxide content of not more than 0.2% by weight A mesoporous silica-alumina material, wherein the weight ratio of the non-ion-exchanged mesoporous silica-alumina material, water and inorganic acid is 1:5-30:0.03-0.3;

[0055] (2) Mix and beat potassium-containing compounds, alkaline earth metal compounds and silicon-aluminum components, then dry them into dry materials, and then roast them at 800°C~1150°C, preferably 900°C~1100°C for 1~10 hours, and then get Potassium-containing gasification active components; wherein the molar ratio of alkaline earth metal compounds in terms of...

preparation Embodiment 1

[0071] The mesoporous material SA-2 was prepared according to the preparation method of the mesoporous material in Example 2 published by CN1565733A.

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Abstract

A multifunctional catalysis composition comprises 1-50wt% of a mesoporous aluminosilicate material, 1-40wt% of a gasification active component, 1-60wt% of a cracking active component, 0-70wt% of clay and 5-97wt% of a heatproof inorganic oxide matrix, wherein the mesoporous aluminosilicate material has a phase structure of pseudo-boehmite, has an anhydrous chemical expression formula of (0-0.3)Na2O.(40-90)Al2O3.(10-60)SiO2 by weight of oxide, and has a specific surface area of 200-400m<2>/g, a pore volume of 0.5-2.0mL/g, an average aperture of 8-20nm and a most probable aperture of 5-15nm The catalysis composition can reduce the gasification temperature of the cracking gasification conversion of hydrocarbon oil.

Description

technical field [0001] The present invention relates to a kind of catalytic composition that is used in petroleum hydrocarbon cracking process and coke gasification combined process produced by cracking, more specifically, relates to a kind of processing and processing petroleum hydrocarbon raw material to produce light Fuel, and a multifunctional catalytic composition for the process of gasifying coke produced in the processing process into hydrogen or syngas with the participation of a gasification agent. Background technique [0002] At present, when catalytic cracking processes heavy and low-quality feedstock oil, it poses challenges to the catalytic cracking process itself and the catalyst. Non-catalytic processing of low-quality heavy oil, including delayed coking, fluidized coking, and flexible coking, has attracted increasing attention. However, the coking process has the problems of high coke yield and low-quality coke that is difficult to utilize. The delayed cokin...

Claims

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Application Information

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IPC IPC(8): B01J29/08B01J29/40B01J29/70B01J35/10C10G11/04C10J3/00
CPCY02P20/52
Inventor 杨雪王子军朱玉霞陈振宇张书红罗一斌汪燮卿
Owner CHINA PETROLEUM & CHEM CORP
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