Catalyst for preparing propylene through olefin disproportionation

A technology for olefin disproportionation and catalysts, applied in physical/chemical process catalysts, molecular sieve catalysts, organic chemistry, etc., can solve problems such as low catalytic activity and low reaction space velocity, and achieve improved diffusion performance, increased specific surface area, and increased dispersion Effect

Active Publication Date: 2008-12-17
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0013] The technical problem to be solved by the present invention is that there are problems in the previous literature that the catalytic activity of the catalyst is low and the reaction space velocity is low, and a new catalyst for the production of propylene by disproportionation of olefins is provided

Method used

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  • Catalyst for preparing propylene through olefin disproportionation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0032] Synthesis of all-silicon MCM-48

[0033] Weigh 10 g of CTAB, dissolve 4.5 g of sodium hydroxide in 286 ml of deionized water, stir at room temperature until clear, and obtain solution A. 47.24 ml of TEOS was slowly added dropwise to A, and vigorously stirred at 30° C. for 1 hour to obtain milky white suspension B. Pour gel B into a stainless steel kettle with a Teflon liner and let it stand in an oven at 100°C for 24 hours. The obtained solid-liquid mixture was suction-filtered, washed with deionized water until neutral, and dried overnight in an oven at 80°C to obtain a synthetic sample.

Embodiment 2

[0035] Direct Synthesis of WOx / MCM-48

[0036] 3.10 g of CTAB and 1.111 g of sodium hydroxide were dissolved in 47 mL of deionized water to obtain a clear solution A. Weigh 8.333 g of 40% (weight) silica sol, slowly drop it into A, stir at 30°C for 5 minutes, then add 1.20 g of ammonium metatungstate, stir vigorously for 1 hour, and obtain white suspension B. Pour gel B into a stainless steel kettle with a Teflon liner and let it stand in an oven at 100°C for 24 hours. The obtained solid-liquid mixture was suction-filtered, washed with deionized water until neutral, and dried overnight in an oven at 80°C to obtain a synthetic sample. Its tungsten content is 12% by weight.

Embodiment 3

[0038] Direct Synthesis of WOx / MCM-48

[0039]3.10 g of CTAB and 1.111 g of sodium hydroxide were dissolved in 47 mL of deionized water to obtain a clear solution A. Weigh 8.333 g of 40% silica sol, slowly drop it into A, stir at 30°C for 5 minutes, then add 0.80 g of ammonium metatungstate, stir vigorously for 1 hour, and obtain white suspension B. Pour the suspension B into a stainless steel kettle with a polytetrafluoroethylene liner, and let it stand in an oven at 100°C for 24 hours. The obtained solid-liquid mixture was suction-filtered, washed with deionized water until neutral, and dried overnight in an oven at 80°C to obtain a synthetic sample. Its tungsten content is 8%.

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Abstract

A catalyst for preparing propene by dismutating olefin is composed of the MCM-48 molecular sieve with 3D crossed arteries used as carrier and the active component chosen from tungsten oxide, molybdenum oxide and rhenium oxide. It has high catalytic activity and reaction space rate.

Description

technical field [0001] The invention relates to a catalyst for producing propylene by olefin disproportionation. Background technique [0002] Olefin disproportionation is a conversion process of olefins. Olefin disproportionation reaction can be used to convert relatively excess and low value-added olefins into high value-added olefin products. [0003] The key to the olefin disproportionation reaction is the catalyst, which can be a homogeneous catalyst or a heterogeneous catalyst. The heterogeneous olefin disproportionation catalyst is generally W, Mo, Re and other compounds supported on an inert carrier. The inert carrier is generally SiO 2 , Al 2 o 3 ,TiO 2 , SiO 2 -Al 2 o 3 , ZrO 2 Aluminophosphate. [0004] US5300718 has reported the process of producing propylene by disproportionation reaction of butene-2 ​​and ethylene, the catalysts used are MgO and WO 3 / SiO 2 mixed bed. [0005] EP0489585 has proposed the preparation method of butene disproportionat...

Claims

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Application Information

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Patent Type & AuthorityPatents(China)
IPC IPC(8): B01J29/06C07C6/04C07C11/06
CPCY02P20/52
Inventor刘苏王仰东徐炜徐舟波杨为民
OwnerCHINA PETROLEUM & CHEM CORP