Method for preparing alumina catalyst, alumina catalyst prepared using same, and method for preparing propylene using alumina catalyst

An alumina and catalyst technology, which is applied in catalyst activation/preparation, carbon compound catalysts, physical/chemical process catalysts, etc., can solve the problems of reduced usefulness of crystalline alumina and reduced specific surface area of ​​alumina dispersants, etc. The effect of improving yield, excellent catalytic activity, and high catalytic activity

Pending Publication Date: 2022-03-08
LG CHEM LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0007] Compared with the crystalline phase alumina obtained by low temperature calcination, the crystalline phase alumina obtained by high temperature calcination has higher stability, but the problem of crystalline phase alumina obtained by calcination at high tem

Method used

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  • Method for preparing alumina catalyst, alumina catalyst prepared using same, and method for preparing propylene using alumina catalyst
  • Method for preparing alumina catalyst, alumina catalyst prepared using same, and method for preparing propylene using alumina catalyst
  • Method for preparing alumina catalyst, alumina catalyst prepared using same, and method for preparing propylene using alumina catalyst

Examples

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Example Embodiment

[0028] The method of preparing an aluminum oxide catalyst of the present invention includes: Step S1: calcining the alumina precursor to form a mixed phase alumina, the mixed phase alumina comprises from 1 to 15% by weight α-alumina, 60 to 95 The weight% θ-alumina, and 4 to 25% by weight of Δ-alumina; step S2: The mixed phase alumina is steam treated with water vapor at a temperature below the primary calcination temperature to activate mixed phase alumina; And step S3: After step S2, secondary calcination is carried out at a temperature higher than the steam processing temperature but below the primary calcination temperature. In this case, it is possible to improve the stability and activity of the alumina catalyst having a compromise based on temperature, and can prepare an alumina catalyst having high mechanical strength and high corrosion / chemical resistance.

[0029] Hereinafter, a method of preparing an aluminum oxide catalyst of the present invention will be gradually des

Example Embodiment

[0088] Example 1

[0089]Burmite was calcined at 1100 ° C for 10 hours under the air atmosphere to obtain a mixed phase oxide of θ-alumina and 20% by weight of δ-alumina by 10% by weight of α-alumina, 70% by weight of θ-alumina and 20% by weight of δ-alumina. . The mixed phase alumina was filled in the tubular reactor, and the temperature of the tubular reactor was set to 400 ° C, and then the steam treatment was performed by supplying water vapor and nitrogen to the reactor. At this time, water vapor is supplied with a rate of 0.026 to 0.1 g / min using an HPLC pump, and a mixture ratio of nitrogen gas and water vapor is supplied with a mass flow controller (MFC) at a rate of 133 ml / min (N. 2 : H 2 The volume ratio of O is 2,500: 1, and the weight ratio of water vapor and mixed phase alumina is from 0.01 to 100: 1. Further, after the steam treatment, calcined at 550 ° C for 5 hours to obtain an alumina catalyst.

Example Embodiment

[0090] Example 2

[0091] This process is carried out in the same manner as in Example 1 except for 6 hours rather than 3 hours during steam treatment.

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Abstract

The present invention relates to a method for preparing an alumina catalyst, an alumina catalyst prepared using the method, and a method for preparing propylene using the alumina catalyst. More specifically, the present invention relates to a method for preparing an alumina catalyst, an alumina catalyst prepared using the method, and a method for preparing propylene using the alumina catalyst, the method for preparing the aluminum oxide catalyst comprises the following steps: S1, performing primary calcination on an aluminum oxide precursor to form mixed-phase aluminum oxide containing 1 to 15 weight percent of alpha-aluminum oxide, 60 to 95 weight percent of theta-aluminum oxide and 4 to 25 weight percent of delta-aluminum oxide; s2, carrying out steam treatment on the mixed-phase aluminum oxide by using water vapor at a temperature lower than the primary calcination temperature so as to activate the mixed-phase aluminum oxide; and S3, after the step S2, carrying out secondary calcination at a temperature higher than the steam treatment temperature and lower than the primary calcination temperature.

Description

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Claims

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Application Information

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Owner LG CHEM LTD
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