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Spherical mesoporous composite material and preparation method thereof and catalyst and preparation method and application thereof

A composite material and mesoporous technology, which is applied in the field of catalyst and its preparation, spherical mesoporous composite material and its preparation, can solve the problems of low propane conversion rate and easy deactivation, achieve stable spherical particle structure, avoid agglomeration, The effect of mesostructure stabilization

Active Publication Date: 2019-02-01
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0006] The process of propane dehydrogenation to propylene has been industrialized for more than 20 years, and there are many studies on dehydrogenation catalysts. However, the current catalysts still have defects such as low propane conversion rate and easy deactivation, which need further improvement and perfection

Method used

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  • Spherical mesoporous composite material and preparation method thereof and catalyst and preparation method and application thereof
  • Spherical mesoporous composite material and preparation method thereof and catalyst and preparation method and application thereof
  • Spherical mesoporous composite material and preparation method thereof and catalyst and preparation method and application thereof

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specific Embodiment approach

[0037] According to a preferred embodiment, the method also includes, in step (1), preparing the component a by a method comprising the following steps:

[0038] In the presence of water, the template agent, the acid agent and the silicon source are first mixed and contacted, and the resulting mixture is crystallized and filtered in sequence.

[0039] Preferably, the templating agent is cetyltrimethylammonium bromide (CTMAB) and / or polyethylene glycol octylphenyl ether (Triton-X100).

[0040] Particularly preferably, the templating agent is cetyltrimethylammonium bromide and polyethylene glycol octylphenyl ether.

[0041] Preferably, the acid agent is hydrochloric acid. There is no particular requirement on the concentration of the hydrochloric acid, for example, it may be 0.1 to 37% by weight. Preferably, the amount of hydrochloric acid is such that the molar ratio of hydrogen chloride to silicon source is (5-50):1.

[0042] Preferably, the silicon source is at least one o...

preparation example 1

[0090] Preparation Example 1: Preparation of Spherical Mesoporous Composite Material C1

[0091] (1) Add CTMAB (4.12mmol) and Triton-X100 (2.46mmol) to hydrochloric acid solution (29.6 grams of 37% concentrated hydrochloric acid and 75 grams of water), mix and stir at 40°C until CTMAB is completely dissolved ; Then tetraethyl orthosilicate (20.91mmol) was added to the above solution, stirred at 40°C for 15h, then stood at 40°C for 24h; the resulting solution was transferred to a polytetrafluoroethylene-lined reactor, After crystallization at 50° C. for 24 hours, filter cake a1 (water content: 5% by weight) containing mesoporous molecular sieves was obtained through filtration and washing.

[0092] (2) 10g water glass (concentration is 15% by weight), 2g sulfuric acid solution (concentration is 12% by weight) and 2g glycerol are mixed, and contact reaction 1.5h at 30 ℃, then use concentration is 98% by weight Sulfuric acid was used to adjust the pH to 3, and then the obtained ...

preparation example 2

[0117] Preparation Example 2: Preparation of Spherical Mesoporous Composite C2

[0118] (1) Add CTMAB (5.50mmol) and Triton-X100 (3.02mmol) to hydrochloric acid solution (29.6 grams of 37% concentrated hydrochloric acid and 90 grams of water), mix and stir at 25°C until CTMAB is completely dissolved ; Then tetraethyl orthosilicate (20.91mmol) was added to the above solution, stirred at 50°C for 15h, and then stood at 50°C for 20h; the resulting solution was transferred to a polytetrafluoroethylene-lined reactor, After crystallization at 60° C. for 20 h, filter and wash to obtain a filter cake a1 containing mesoporous molecular sieves (water content: 6% by weight).

[0119] (2) 20g water glass (concentration is 15% by weight), 2g sulfuric acid solution (concentration is 12% by weight) and 2g glycerol are mixed, and contact reaction 1.5h at 30 ℃, then with concentration is 98% by weight Sulfuric acid was used to adjust the pH to 4, and then the obtained reaction material was su...

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Abstract

The invention relates to the field of catalysts, and discloses a spherical mesoporous composite material and a preparation method thereof, as well as a catalyst and a preparation method and application thereof. The spherical mesoporous composite material is 10-30 microns in average particle diameter, 100-300 m<2> / g in specific surface area and 0.5-1.5 mL / g in pore volume, and the pore diameter shows a two-peak distribution, the most probable pore diameters corresponding to the two peaks are 1-3 nanometers and 20-60 nanometers, respectively, and the spherical mesoporous composite material contains mesoporous molecular sieves and silica gels. The spherical mesoporous composite material is small in particle size, uniform in particle size distribution, stable in mesoporous structure and narrowin particle size distribution curve, which can avoid agglomeration of mesoporous materials in the use process, improve the fluidity and bring convenience to storage, transportation, post-processing and application of mesoporous materials.

Description

technical field [0001] The invention relates to the field of catalysts, in particular to a spherical mesoporous composite material and a preparation method thereof, a catalyst containing the spherical mesoporous composite material, a preparation method and application thereof. Background technique [0002] Propylene is the basic raw material of petrochemical industry, mainly used in the production of polypropylene, acrylonitrile, acetone, propylene oxide, acrylic acid and butyl octanol. Half of the propylene supply comes from refinery by-products, with about 45% from steam cracking and a small amount from other alternative technologies. [0003] In recent years, the demand for propylene has been increasing year by year, and the traditional propylene production can no longer meet the demand for propylene in the chemical industry. Therefore, increasing the production of propylene has become a hot research topic. Among them, propane dehydrogenation to propylene is a major tech...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J35/08B01J29/03C07C5/333C07C11/06B01J35/10
CPCC07C5/3332B01J29/0325C07C2529/03B01J2229/18B01J35/51B01J35/643B01J35/638B01J35/615B01J35/651B01J35/69B01J35/635B01J35/647C07C11/06Y02P20/52
Inventor 亢宇刘红梅张明森
Owner CHINA PETROLEUM & CHEM CORP