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Catalysts for Butene Disproportionation

A catalyst and butene technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, organic chemistry, etc., can solve the problem of low disproportionation activity of catalysts, and achieve good disproportionation activity and conversion rate Improved, synergistic effect

Active Publication Date: 2018-04-06
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0018] The technical problem to be solved by the present invention is the problem of low catalyst disproportionation activity existing in the prior art, and a new catalyst for butene disproportionation is provided

Method used

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  • Catalysts for Butene Disproportionation
  • Catalysts for Butene Disproportionation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0037] 51.999 grams of chromatographic silica gel, 100 grams of silica sol (containing 40% by weight of silicon oxide) and 2 grams of turnip powder were mixed and put into a blender, and after stirring for 20 minutes, 0.003 grams of titanium tetrachloride and 10 grams of partial Ammonium tungstate (containing 80% by weight of tungsten oxide), after stirring for 5 minutes, add 250 grams of deionized water, knead for 2 hours, extrude and dry at 100°C for 4 hours, and bake at 550°C for 4 hours in air atmosphere The obtained catalyst is denoted as SL-1.

[0038] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, using 2-butene and ethylene as raw materials, calculated by mass fraction, the raw materials were 99.9% of 2-butene and 99.9% of ethylene. The reaction is at a temperature of 300°C, a pressure of 3MPa, a molar ratio of ethylene to butene of 3.5 and a weight space velocity of 2-butene of 8 hours -1 The evaluation was carried o...

Embodiment 2

[0040] 47 grams of chromatographic silica gel, 100 grams of silica sol (containing 40% by weight of silicon oxide) and 2 grams of turnip powder were mixed and put into a blender, and after stirring for 20 minutes, 11.85 grams of titanium tetrachloride and 10 grams of partial Ammonium tungstate (containing 80% by weight of tungsten oxide), after stirring for 5 minutes, add 250 grams of deionized water, knead for 2 hours, extrude and dry at 100°C for 4 hours, and bake at 550°C for 4 hours in air atmosphere The obtained catalyst is denoted as SL-2.

[0041] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, using 2-butene and ethylene as raw materials, calculated by mass fraction, the raw materials were 99.9% of 2-butene and 99.9% of ethylene. The reaction is at a temperature of 300°C, a pressure of 3MPa, a molar ratio of ethylene to butene of 3.5 and a weight space velocity of 2-butene of 8 hours -1 The evaluation was carried out u...

Embodiment 3

[0043] 51.998 grams of chromatographic silica gel, 100 grams of silica sol (containing 40% by weight of silicon oxide) and 2 grams of scallop powder were mixed and put into a blender, and after stirring for 20 minutes, 0.005 grams of titanium tetrachloride and 10 grams of partial Ammonium tungstate (containing 80% by weight of tungsten oxide), after stirring for 5 minutes, add 250 grams of deionized water, knead for 2 hours, extrude and dry at 100°C for 4 hours, and bake at 550°C for 4 hours in air atmosphere The obtained catalyst is designated as SL-3.

[0044] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, using 2-butene and ethylene as raw materials, calculated by mass fraction, the raw materials were 99.9% of 2-butene and 99.9% of ethylene. The reaction is at a temperature of 300°C, a pressure of 3MPa, a molar ratio of ethylene to butene of 3.5 and a weight space velocity of 2-butene of 8 hours -1 The evaluation was carri...

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Abstract

The present invention relates to a catalyst for butene disproportionation, which mainly solves the problem of low catalyst disproportionation activity existing in the prior art. The present invention adopts a catalyst for butene disproportionation, which, in weight percentage, comprises the following components: a) 1-30% of tungsten element or its oxide, b) 0.001-5% of tungsten element selected from periodic table IVB At least one element in the group or its oxide, c) the technical scheme of 65-99% silicon oxide or aluminum oxide, can solve the problem well, and can be used for the industrial production of butene disproportionation reaction.

Description

technical field [0001] The present invention relates to a catalyst for the disproportionation of butenes. Background technique [0002] The traditional methods of ethylene co-production and refinery recovery of propylene are obviously difficult to meet the growing demand for propylene. The use of olefin disproportionation technology can digest C without reducing the cracking severity of naphtha. 4 Distillate, and can increase the production of propylene, so the research and development of olefin disproportionation to propylene technology is not only to improve the production of propylene, but also to promote low value-added C 4 The comprehensive utilization of distillates is of great significance, among which the disproportionation of butene involved in the present invention to produce propylene is a promising process. [0003] Olefin disproportionation reaction, also known as olefin double bond replacement reaction, is an olefin conversion phenomenon discovered in the 1960...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/30C07C6/04C07C11/06C07C11/107
CPCY02P20/52
Inventor 刘苏宣东董静
Owner CHINA PETROLEUM & CHEM CORP