Unlock instant, AI-driven research and patent intelligence for your innovation.

Propane dehydrogenation catalyst and preparation method thereof and method for preparing propylene by propane dehydrogenation

A propane dehydrogenation and catalyst technology, applied in the direction of catalyst activation/preparation, molecular sieve catalysts, chemical instruments and methods, etc., can solve problems such as easy deactivation, low propane conversion rate, low propylene selectivity, and unstable mesopore structure. Achieve the effect of appropriate pore size, uniform distribution of pore structure and good structural stability

Active Publication Date: 2019-05-14
CHINA PETROLEUM & CHEM CORP +1
View PDF8 Cites 6 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The purpose of the present invention is to overcome the unstable mesoporous structure in the prior art, which further leads to defects such as low propane conversion rate and propylene selectivity and easy deactivation, and to provide a propane dehydrogenation catalyst and its preparation method and propane dehydrogenation catalyst. Hydrogen to propylene method

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • Propane dehydrogenation catalyst and preparation method thereof and method for preparing propylene by propane dehydrogenation
  • Propane dehydrogenation catalyst and preparation method thereof and method for preparing propylene by propane dehydrogenation
  • Propane dehydrogenation catalyst and preparation method thereof and method for preparing propylene by propane dehydrogenation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0063] This example is used to illustrate the propane dehydrogenation catalyst and its preparation method.

[0064] (1) Preparation of the carrier

[0065] Cetyltrimethylammonium bromide and tetraethyl orthosilicate are added in the ammonia solution that the concentration is 25% by weight, wherein, the add-on of tetraethylorthosilicate is 1g, and the molar feeding ratio is ethyl orthosilicate. Ester: cetyl trimethyl ammonium bromide: ammonia water (25%): deionized water = 1: 0.37: 2.8: 142, stirred at 80 °C until dissolved, the solution was suction filtered and the mesoporous material was filtered. The filter cake is washed to pH 7 to obtain a mesoporous molecular sieve filter cake A1 with a two-dimensional hexagonal pore structure;

[0066] The water glass with a concentration of 15% by weight and the sulfuric acid solution with a concentration of 12% by weight and n-butanol are fully reacted at 30 ° C for 1.5 hours according to the weight ratio of water glass: sulfuric acid...

Embodiment 2

[0094] This example is used to illustrate the propane dehydrogenation catalyst and its preparation method.

[0095] (1) Preparation of the carrier

[0096] Cetyltrimethylammonium bromide and tetraethyl orthosilicate are added in the ammonia solution that the concentration is 25% by weight, wherein, the add-on of tetraethylorthosilicate is 1g, and the molar feeding ratio is ethyl orthosilicate. Ester: cetyl trimethyl ammonium bromide: ammonia water (25%): deionized water = 1: 0.5: 3.5: 150, stirred at 80 °C until dissolved, the solution was suction filtered and the mesoporous material was filtered. The filter cake was washed to a pH of 7 to obtain a mesoporous molecular sieve filter cake A2 with a two-dimensional hexagonal pore structure;

[0097] The water glass with a concentration of 15% by weight, a sulfuric acid solution with a concentration of 12% by weight and n-butanol, and the water glass: sulfuric acid: n-butanol weight ratio = 6: 1: 1 were fully reacted at 60 ° C fo...

Embodiment 3

[0108] This example is used to illustrate the propane dehydrogenation catalyst and its preparation method.

[0109] Cetyltrimethylammonium bromide and tetraethyl orthosilicate are added in the ammonia solution that the concentration is 25% by weight, wherein, the add-on of tetraethylorthosilicate is 1g, and the molar feeding ratio is ethyl orthosilicate. Ester: cetyl trimethyl ammonium bromide: ammonia water (25%): deionized water = 1: 0.4: 3: 130, stirred at 60 °C until dissolved, the solution was suction filtered and the mesoporous material was filtered. The filter cake is washed to a pH of 7 to obtain a mesoporous molecular sieve filter cake A3 with a two-dimensional hexagonal pore structure;

[0110] Water glass with a concentration of 15 wt %, sulfuric acid solution with a concentration of 12 wt % and n-butanol, and the water glass: sulfuric acid: n-butanol weight ratio = 3: 1: 1 were fully reacted at 10 ° C for 5 h, The pH of sulfuric acid with a concentration of 98% by...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

PUM

PropertyMeasurementUnit
compressive strengthaaaaaaaaaa
particle sizeaaaaaaaaaa
specific surface areaaaaaaaaaaa
Login to View More

Abstract

The invention relates to the field of catalysts and discloses a propane dehydrogenation catalyst. The propane dehydrogenation catalyst comprises a supporter, a Pt component, a Sn component and a Na component, and the Pt component, a Sn component and a Na component are supported on the supporter. The supporter is made of a spherical bi-porous aluminum-containing silica gel and mesoporous molecularsieve composite material which contains an aluminum component, a mesoporous molecular sieve material in a two-dimensional hexagonal pore passage structure and silica gel. The spherical bi-porous aluminum-containing silica gel and mesoporous molecular sieve composite material is characterized in that the compressive strength is 12-16MPa, the average particle size is 20-80micron, the specific surface area is 100-200m<2> / g, the pore volume is 0.5-1.5mL / g, the pore diameter is in bimodal distribution, and most probable pore diameters corresponding to two modes are 0.3-5nm and 30-40nm respectively.The propane dehydrogenation catalyst applied to reaction of propane dehydrogenation for preparing propylene shows excellent catalytic performance, and high propane conversion rate, high propylene selectivity, high catalyst stability and great anti-poisoning performance are realized.

Description

technical field [0001] The present invention relates to the field of catalysts, in particular, to a propane dehydrogenation catalyst, a preparation method thereof, and a method for producing propylene from propane dehydrogenation. 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 dehydrogenation to propylene is a major technology for increasing propylene production. For more than 10 years, pr...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to View More

Application Information

Patent Timeline
no application Login to View More
Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/03B01J35/02B01J35/08B01J35/10B01J37/02C07C5/333C07C11/06B01J35/00
CPCY02P20/52
Inventor 亢宇刘红梅张明森
Owner CHINA PETROLEUM & CHEM CORP