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A kind of preparation method of sulfurized dehydrogenation catalyst

A dehydrogenation catalyst, catalyst technology, applied in catalyst activation/preparation, physical/chemical process catalysts, chemical instruments and methods, etc., can solve the problems affecting the production efficiency and long time of production equipment

Active Publication Date: 2011-11-30
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The pre-sulfurization method of the dehydrogenation catalyst in the prior art mainly adopts pre-sulfurization in the reactor, the catalyst is loaded into the reactor, and then the vulcanizing agent is introduced for vulcanization. The main disadvantage is that the time is long, which affects the production efficiency of the production device.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

example 1

[0021] Prepare an alumina support containing La and Sn. The 1.0M aluminum trichloride solution, 0.01M tin tetrachloride solution and 0.01M La(NO 3 ) 3 The solution is mixed, and the precipitation reaction is carried out with 10% ammonia water by weight concentration. The precipitation reaction temperature is 60~80℃, the pH value is controlled at 7.0~9.0, after filtration, water washing and acidification, the oil ammonia column is pressurized into balls, dried and aged And calcined at 650°C for 4 hours to obtain alumina pellets containing 0.5 wt% La and 0.4 wt% Sn. When preparing other alumina supports with different La and Sn contents, the amount of various raw materials can be adjusted appropriately.

[0022] The calcined carrier is immersed in an aqueous solution containing chloroplatinic acid at 70°C for 6 hours, dried at 120°C for 5 hours, then calcined at 500°C for 4 hours, and activated in air containing water vapor for 4 hours. And then at 70℃ with KNO 3 Immersed in the a...

example 2

[0026] Prepare an alumina support containing La and Sn. The 1.03M aluminum trichloride solution, 0.02M tin tetrachloride solution and 0.03M La(NO 3 ) 3 After the solution is mixed, add 11% by weight ammonia water, mix well in a neutralization tank at 60-80℃, control the pH value of 7.0-9.0, filter, wash, and acidify, pressurize the oil ammonia column into a ball, After drying, aging, and calcining at 750°C for 4 hours, alumina pellets containing 1.0 wt% La and 2.0 wt% Sn are obtained.

[0027] The calcined carrier is immersed in an aqueous solution containing chloroplatinic acid at 70°C for 6 hours, dried at 120°C for 5 hours, then calcined at 500°C for 4 hours, and activated in air containing water vapor for 4 hours. And then at 70℃ with KNO 3 And immersed in the aqueous solution for 2h, dried, roasted under the same conditions, and then immersed (NH 4 ) 2 The S solution was reduced in hydrogen at 500°C for 4 hours to obtain a catalyst. The loading amount of each component in t...

example 3

[0031] Prepare an alumina support containing La and Sn. The 0.96M aluminum trichloride solution, 0.01M tin tetrachloride solution and 0.02M La(NO 3 ) 3 After the solution is mixed, add 11% ammonia water with a weight concentration, mix it evenly in a neutralization tank at 60~80℃, control the pH value of 7.0~9.0, filter, wash and acidify, pressurize the oil ammonia column into a ball, pass After drying, aging, and calcining at 700°C for 4 hours, alumina pellets containing 1.5 wt% La and 1.0 wt% Sn are obtained.

[0032] The calcined carrier is immersed in an aqueous solution containing chloroplatinic acid at 70°C for 6 hours, dried at 120°C for 5 hours, then calcined at 500°C for 4 hours, and activated in air containing water vapor for 4 hours. And then at 70℃ with KNO 3 And immersed in the aqueous solution for 2h, dried, roasted under the same conditions, and then immersed (NH 4 ) 2 The S solution was reduced in hydrogen at 500°C for 4 hours to obtain a catalyst. The loading am...

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PUM

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Abstract

The invention discloses a method for preparing a vulcanized dehydrogenation catalyst. The method comprises the following steps of: preparing an La and Sn-containing aluminum oxide carrier; dipping dehydrogenation active ingredients; performing vapor dechlorination process; and injecting a sulfur-containing compound and drying the carrier to obtain the dehydrogenation catalyst. The dehydrogenation catalyst prepared by the method has the advantages of high activity stability, long service life, high regeneration and the like when used for propane dehydrogenation and is particularly applicable to a technological process for preparing the propane by the propane dehydrogenation.

Description

Technical field [0001] The invention relates to a preparation method of a catalyst for preparing olefins by the dehydrogenation of alkane, in particular to a preparation method of the catalyst for the reaction activity and stability of the catalyst for preparing propylene by the dehydrogenation of propane. Background technique [0002] Since the beginning of the new century, the world's demand for petrochemical raw materials and petrochemical products will continue to grow. The demand for propylene as the basic petrochemical raw material will continue to grow. However, the ability of conventional steam cracking and FCC technology to produce propylene cannot meet the rapidly growing demand, making it the market There is a global shortage. Moreover, with the increasing scarcity of petroleum resources, the production of propylene has shifted from relying solely on petroleum as a raw material to a diversified technical route of raw material sources, especially the technical route of ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J27/045B01J37/00C07C5/333C07C11/06
CPCY02P20/52
Inventor 张海娟李江红金亮张喜文宋喜军
Owner CHINA PETROLEUM & CHEM CORP