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Molecular sieve catalyst for catalyzing hydrocarbon cracking to produce propylene and its preparation method and use

A technology for catalyzing hydrocarbons and molecular sieves, applied in the direction of molecular sieve catalysts, including molecular sieve catalysts, carbon compound catalysts, etc., can solve the problems of low propylene selectivity, impossibility to improve, high ethylene selectivity, etc., achieve simple and easy preparation method, improve propylene yield The effect of high efficiency and easy raw materials

Active Publication Date: 2022-07-26
HENAN UNIVERSITY
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

For hydrocarbons in naphtha, the number of secondary carbon atoms is the largest, therefore, it is easy to lead to high selectivity of ethylene in unimolecular cracking products, while the selectivity of propylene is relatively low
Even if the cracking depth is suppressed by improving the molecular sieve pore distribution or acidity distribution, it can only increase the selectivity of ethylene and propylene in the product at the same time, without selectivity, that is, the n(propylene) / n(ethylene) in the product cannot be increased

Method used

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  • Molecular sieve catalyst for catalyzing hydrocarbon cracking to produce propylene and its preparation method and use
  • Molecular sieve catalyst for catalyzing hydrocarbon cracking to produce propylene and its preparation method and use
  • Molecular sieve catalyst for catalyzing hydrocarbon cracking to produce propylene and its preparation method and use

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preparation example Construction

[0053] A first aspect of the present invention provides a method for preparing a molecular sieve catalyst for catalyzing hydrocarbon cracking to produce propylene, comprising the following steps:

[0054] A precursor solution is obtained after mixing a silicon source, a templating agent and an optional aluminum source in a solvent; the precursor solution is subjected to hydrothermal crystallization to obtain a hydrothermally crystallized product. Then, the product is washed with deionized water until neutral, and the hydrothermally crystallized product is calcined to obtain a molecular sieve catalyst precursor. The molecular sieve precursor is subjected to ammonium exchange, dried, and then calcined to obtain a molecular sieve carrier.

[0055] The obtained molecular sieve is used as the carrier, the aluminum-containing solution is used as the precursor of the metal solution, and the aluminum is loaded on the molecular sieve carrier by the equal volume impregnation method; the...

Embodiment 1~5

[0087] 8.32g tetraethyl orthosilicate (TOES), 13.0g tetrapropylammonium hydroxide (TPAOH) (25wt% aqueous solution), certain mass of aluminum sulfate (Al 2 (SO 4 ) 3 ·18H 2 O) and 25.16 g of deionized water were configured to obtain a mixed solution. The mixed solution was stirred at room temperature for 24 hours to obtain a crystallized solution. The crystallized solution was placed in a crystallization kettle, and hydrothermally crystallized at 165 °C for 3 days to obtain a hydrothermally crystallized product; the synthesized hydrothermal The crystallized product powder was washed with deionized water until neutral, dried at 120°C, and calcined at 550°C for 6 hours in a muffle furnace air atmosphere to obtain the ZSM-5 molecular sieve precursor. Weigh 1 g of ZSM-5 molecular sieve precursor and 125 mL of 1 mol / L NH 4 The Cl solution was mixed, heated in a water bath at 85°C, stirred for 3h, washed with deionized water until neutral, dried at 120°C for 6h, and calcined at 5...

Embodiment 1

[0088] The mass of aluminum sulfate used in Example 1 was 0.1 g, and the theoretical n(Si) / n(Al) of the obtained molecular sieve was 150.

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Abstract

The invention discloses a molecular sieve catalyst for catalyzing hydrocarbon cracking to prepare propylene, a preparation method and application thereof, and belongs to the field of catalysts. In the present invention, quantitative non-framework aluminum is introduced into the ZSM-5 molecular sieve by an equal volume impregnation method, and thanks to the fact that Al itself is also a component in the molecular sieve framework, secondary Al element is carried out in the ZSM-5 molecular sieve catalyst whose Al concentration has been synthesized and determined. Modification can realize the precise regulation of the Al content outside the ZSM-5 molecular sieve framework. By changing the introduction amount of Al element, quantitatively constructing extra-framework Al-OH can realize the controllable modulation of acid content, and then achieve the purpose of high-yield propylene in hydrocarbon cracking reaction. In addition, the preparation method of the present invention is simple and feasible, and the raw materials are easy to obtain.

Description

technical field [0001] The invention relates to a molecular sieve catalyst and a preparation method and application thereof, in particular to a kind of precise controllable The invention relates to a ZSM-5 molecular sieve catalyst with an acid molar ratio, which can be specifically used for catalyzing the cracking of hydrocarbons to prepare propylene, and belongs to the field of catalysts. Background technique [0002] The widespread use of polypropylene worldwide in recent years has led to an increasing demand for the raw material propylene. In the past, the production of propylene was mainly obtained through the co-production of naphtha steam cracking process, but the low-carbon olefins produced by this route were mainly ethylene, and the supply of propylene was far from meeting the needs of society. And steam cracking technology is often carried out at relatively high temperature (>750°C), resulting in a large amount of carbon dioxide emissions and a prominent greenh...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J29/40C07C4/06C07C11/06C01B39/40
CPCB01J29/40C07C4/06C01B39/40B01J2229/186C07C2529/40C01P2004/03C01P2002/72C01P2004/62C01P2006/12C01P2006/14C07C11/06Y02P20/52C10G2400/20C10G11/05B01J35/1042B01J35/1019B01J21/02B01J37/08B01J29/70B01J35/026B01J37/0236B01J37/031B01J37/04B01J37/06B01J37/30B01J2229/20B01J2229/38C07C2529/70
Inventor 田亚杰何新宇乔聪震
Owner HENAN UNIVERSITY