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metathesis catalyst

A technology for metathesis catalyst and oxide, which is used in metathesis reaction to produce hydrocarbons, physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, etc. It can solve the problems of low catalyst disproportionation activity and achieve good disproportionation activity. , the effect of improving life expectancy and conversion rate

Active Publication Date: 2017-06-20
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0020] 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 metathesis catalyst is provided

Method used

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Examples

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Effect test

Embodiment 1

[0035] 51.9986 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 12 minutes, 0.0002 gram of ammonium dimolybdate (containing 84% by weight) was added. % of molybdenum oxide), 0.0003 gram of ferric nitrate, 0.0001 gram of sodium oxide, 0.001 gram of calcium oxide, 0.0004 gram of aluminum nitrate and 10 gram of ammonium metatungstate (containing 80% by weight of tungsten oxide), and then add 250 grams of tungsten after stirring for 5 minutes Deionized water, kneading for 2 hours, extruding, drying at 100°C for 4 hours, and calcining at 550°C for 4 hours in air atmosphere to obtain the catalyst, which is designated as SL-1.

[0036] 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% 2-butene ...

Embodiment 2

[0038] 51.9977 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 12 minutes, 0.002 gram of ammonium dimolybdate (containing 84% by weight) was added. % of molybdenum oxide), 0.0003 gram of ferric nitrate, 0.0001 gram of sodium oxide, 0.001 gram of calcium oxide, 0.0004 gram of aluminum nitrate and 10 gram of ammonium metatungstate (containing 80% by weight of tungsten oxide), and then add 250 grams of tungsten after stirring for 5 minutes Deionized water, kneading for 2 hours, extruding, drying at 100°C for 4 hours, and calcination at 550°C for 4 hours in air atmosphere to obtain the catalyst, which is designated as SL-2.

[0039] The evaluation conditions of the catalyst are the same as in Example 1, and the evaluation results are shown in Table 1.

Embodiment 3

[0041] 51.4987 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 12 minutes, 0.59 gram of ammonium dimolybdate (containing 84% by weight) was added. % of molybdenum oxide), 0.0003 gram of ferric nitrate, 0.0001 gram of sodium oxide, 0.001 gram of calcium oxide, 0.0004 gram of aluminum nitrate and 10 gram of ammonium metatungstate (containing 80% by weight of tungsten oxide), and then add 250 grams of tungsten after stirring for 5 minutes Deionized water, kneading for 2 hours, extruding, drying at 100°C for 4 hours, and calcination at 550°C for 4 hours in air atmosphere to obtain the catalyst, which is designated as SL-3.

[0042] The evaluation conditions of the catalyst are the same as in Example 1, and the evaluation results are shown in Table 1.

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Abstract

The invention relates to a metathesis catalyst, which mainly solves the problem of low disproportionation activity of the catalyst in the prior art. The present invention adopts a metathesis catalyst, which comprises the following components in parts by weight: a) 1-30 parts of tungsten element or its oxide; b) 0.0001-1 part of molybdenum element or its oxide; c) 0.0001- 1 part of iron element or its oxide; d) 0.0001-1 part of alkali metal element or its oxide; e) 0.001-20 parts of alkaline earth metal element or its oxide; f) 0.0001-7 parts of aluminum element or its oxide; g) The technical solution of 40-99 parts silicon oxide solves this problem well and can be used in the industrial production of olefin disproportionation reaction.

Description

technical field [0001] The invention relates to a metathesis catalyst, especially a metathesis catalyst for olefin disproportionation reaction. 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 conver...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/888C07C11/06C07C6/04
CPCY02P20/52
Inventor 董静宣东刘苏
Owner CHINA PETROLEUM & CHEM CORP