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Supported catalyst, preparation method and application thereof, and method for producing propylene from propane dehydrogenation

A supported catalyst and catalyst technology, applied in catalyst activation/preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of uneven dispersion of active metal components, complex preparation process, etc., and achieve catalyst stability. Good, simple preparation process, easy control of conditions

Active Publication Date: 2020-09-15
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0004] The purpose of the present invention is to overcome the defects of complex preparation process and uneven dispersion of active metal components in the existing dehydrogenation catalyst, and provide a supported catalyst and its preparation method and application

Method used

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  • Supported catalyst, preparation method and application thereof, and method for producing propylene from propane dehydrogenation
  • Supported catalyst, preparation method and application thereof, and method for producing propylene from propane dehydrogenation
  • Supported catalyst, preparation method and application thereof, and method for producing propylene from propane dehydrogenation

Examples

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Embodiment approach

[0026] According to a preferred embodiment of the present invention, the process of mixing and contacting comprises: (1) mixing cetyl trimethyl ammonium bromide (CTAB), polyethylene glycol octyl phenyl ether (Triton X -100) and hydrochloric acid were stirred at 25-60°C until dissolved; (2) the solution obtained in step (1) and silicate ester were stirred at 25-60°C for 10-72 hours, and allowed to stand for 10-72 hours.

[0027] In the present invention, the preparation method of the carrier preferably further includes washing and drying processes after the filtration. The washing and drying processes can be conventional choices in the field, and are not repeated here.

[0028] In the present invention, the template agent can be removed by washing and / or calcination. The washing can be water washing and / or alcohol washing, and the conditions for washing and removing the template agent include: the temperature can be 90-120° C., and the time can be 10-40 hours. According to a ...

Embodiment 1

[0059] This example is used to illustrate the supported catalyst provided by the present invention and its preparation method and the method for producing propylene by dehydrogenation of propane

[0060] (1) Preparation of the carrier

[0061] 1.5 grams of CTAB (hexadecyltrimethylammonium bromide) and 1.5 ml of polyethylene glycol octyl phenyl ether (Triton-X100) were added to 29.6 grams of 37% by weight concentrated hydrochloric acid and 75 grams In hydrochloric acid composed of water, mix and stir at 40°C until CTAB is completely dissolved; then add 4.35 grams of ethyl orthosilicate to the above solution, stir at 40°C for 15 minutes, and stand at 40°C for 24 hours. Then filter, wash and dry to obtain the original powder mesoporous material. The above-mentioned raw powder mesoporous material was calcined at 600° C. for 24 hours to remove the template agent to obtain spherical mesoporous material A1.

[0062] The spherical mesoporous material A-1 was characterized by X-ray d...

Embodiment 2

[0073] This example is used to illustrate the supported catalyst provided by the present invention and its preparation method and the method for producing propylene by dehydrogenation of propane

[0074] (1) Preparation of the carrier

[0075] 1.125 grams of CTAB (hexadecyltrimethylammonium bromide) and 3.75 ml of polyethylene glycol octyl phenyl ether (Triton-X100) were added to 20.6 grams of 37 wt% concentrated hydrochloric acid and 62.2 grams In hydrochloric acid composed of water, mix and stir at 40 °C until CTAB is completely dissolved; then add 4.35 grams of ethyl orthosilicate to the above solution, stir at 40 °C for 15 minutes to dissolve, and then stand at 40 °C for 24 Hour. Then filter, wash and dry to obtain the original powder mesoporous material. The above-mentioned raw powder mesoporous material was washed with ethanol under the condition of refluxing at 100° C. for 24 hours, and the template agent was removed to obtain spherical mesoporous material A2.

[007...

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Abstract

The invention relates to the field of catalysts, and discloses a supported catalyst and a preparation method thereof. The supported catalyst is used in the reaction of propane dehydrogenation to prepare propylene, and a method of propane dehydrogenation to prepare propylene. The supported catalyst includes a carrier and a platinum component, a tin component and a sodium component supported on the carrier, wherein the carrier is a spherical mesoporous material, and the average particle size of the spherical mesoporous material is 3 ‑20μm, specific surface area 1000‑2000m 2 / g, the pore volume is 0.5-1.5 ml / g, and the pore diameter is 1-3nm. When the supported catalyst of the present invention is used to catalyze the reaction of propane dehydrogenation to propylene, the propane conversion rate is high and the propylene selectivity is high.

Description

technical field [0001] The invention relates to the field of catalysts, in particular, to a supported catalyst, a method for preparing a supported catalyst, an application of the supported catalyst in the reaction of preparing propylene by dehydrogenation of propane, and a method for preparing propylene by dehydrogenating propane . Background technique [0002] Propylene is the basic raw material of petrochemical industry and is mainly used to produce polypropylene, acrylonitrile, acetone, propylene oxide, acrylic acid and butanol. Half of the propylene supply comes from refinery by-products, and about 45% comes from steam cracking, with a small amount of other alternative technologies. In recent years, the demand for propylene has increased year by year, and traditional propylene production has been unable to meet the demand for propylene in the chemical industry. Therefore, increasing propylene production has become a major research focus. Among them, propane dehydrogena...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/62B01J35/10B01J35/08B01J37/02B01J37/08C07C5/333C07C11/06
CPCC07C5/3332B01J23/002B01J23/626B01J37/0209B01J37/08B01J2523/00B01J35/51B01J35/618B01J35/60B01J35/638B01J35/643B01J35/635B01J35/647C07C11/06B01J2523/12B01J2523/41B01J2523/43B01J2523/828Y02P20/52
Inventor 亢宇刘红梅张明森
Owner CHINA PETROLEUM & CHEM CORP