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Method for producing tetramethylethylene by disproportionation of isobutene

A technology of tetramethylethylene and isobutylene, applied in chemical instruments and methods, organic chemistry, hydrocarbons and other directions, can solve the problem of low selectivity of target products, achieve increased weight selectivity, good technical effect, and improved selectivity Effect

Active Publication Date: 2016-12-28
CHINA PETROLEUM & CHEM CORP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0020] The technical problem to be solved by the present invention is the problem of low selectivity of the target product existing in the prior art, and a new method for preparing tetramethylethylene by disproportionation of isobutene is provided

Method used

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  • Method for producing tetramethylethylene by disproportionation of isobutene
  • Method for producing tetramethylethylene by disproportionation of isobutene
  • Method for producing tetramethylethylene by disproportionation of isobutene

Examples

Experimental program
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Effect test

Embodiment 1

[0039] A solution containing 18.6 grams of diammonium hydrogen phosphate and 940 grams of γ-Al 2 o 3 Mix evenly and put it in a blender, add 10 grams of asparagus powder and stir for 12 minutes, then add 61.3 grams of ammonium dimolybdate, then add 2.5 kilograms of deionized water, knead for 0.5 hours and then extrude, and put the extruded catalyst at 100 ° C Dry at 550°C for 3 hours, and bake at 550°C for 4 hours to obtain a finished catalyst, which is designated as SL-1.

[0040] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, and the raw material was 99.9% isobutene in terms of mass fraction. The reaction is at a temperature of 120°C, a pressure of 0.6MPa in absolute pressure, and a weight space velocity of isobutylene of 4 hours -1 Under the conditions, the evaluation results are shown in Table 1.

Embodiment 2

[0042] A solution containing 37.2 grams of diammonium hydrogen phosphate and 900 grams of γ-Al 2 o 3 Mix evenly and put it in a mixer, add 10 grams of scallop powder and stir for 12 minutes, then add 98 grams of ammonium dimolybdate and 10 grams of ammonium metatungstate, then add 2.5 kg of deionized water, knead for 0.5 hours and then extrude into strips. The strip-shaped catalyst was dried at 100°C for 3 hours and calcined at 550°C for 4 hours to obtain a finished catalyst, which was designated as SL-2.

[0043] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, and the raw material was 99.9% isobutene in terms of mass fraction. The reaction is at a temperature of 120°C, a pressure of 0.6MPa in absolute pressure, and a weight space velocity of isobutylene of 4 hours -1 Under the conditions, the evaluation results are shown in Table 1.

Embodiment 3

[0045] A solution containing 55.8 grams of diammonium hydrogen phosphate and 820 grams of γ-Al 2 o 3 Mix evenly and put it in a blender, add 10 grams of asparagus powder and stir for 12 minutes, then add 183.9 grams of ammonium dimolybdate, then add 2.5 kilograms of deionized water, knead for 0.5 hours and then extrude, and put the extruded catalyst at 100 ° C Dry at 550°C for 3 hours, and bake at 550°C for 4 hours to obtain a finished catalyst, which is designated as SL-3.

[0046] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, and the raw material was 99.9% isobutene in terms of mass fraction. The reaction is at a temperature of 120°C, a pressure of 0.6MPa in absolute pressure, and a weight space velocity of isobutylene of 4 hours -1 Under the conditions, the evaluation results are shown in Table 1.

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Abstract

The invention relates to a method for preparing tetramethylethylene by disproportionation of isobutene, and mainly solves the problem of low selectivity of target products existing in the prior art. The present invention adopts isobutylene as raw material, in a fixed bed reactor, the reaction temperature is 80-200 DEG C, the reaction pressure is 0.2-0.8MPa, and the weight space velocity is 1-20 hours ‑1 Under the condition, the raw material and the catalyst contact reaction to generate the effluent containing tetramethyl ethylene, wherein the catalyst used is in parts by weight, including the following components: a) 5~49 parts of molybdenum oxide; b) 1~8 parts of pentoxides The technical scheme of diphosphorus, c) 50-94 parts of alumina carrier, solves the problem well, and can be used for the industrial production of isobutylene disproportionation to prepare tetramethyl ethylene.

Description

technical field [0001] The invention relates to a method for preparing tetramethylethylene by disproportionation of isobutene. Background technique [0002] Olefin disproportionation (Olefin metathesis) is a conversion process of olefins. Under the action of transition metal catalysts (such as W, Mo, Re, etc.), the C=C double bond in olefins is broken and re-formed, so that new olefin products can be obtained. [0003] As early as 1931, when Schneider and Frolich cracked propylene at 1130K, they observed that ethylene and butene appeared in the product. This was the first report on the phenomenon of olefin disproportionation; (MoO 3 / Al 2 o 3 ) and propylene disproportionation under the action of homogeneous catalysts. Since then, a lot of research work has shown that numerous transition metal compounds have catalytic activity for olefin disproportionation, among which W, Mo and Re have the best catalytic performance. [0004] In the 1960s, the disproportionation react...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C07C11/107C07C2/00
Inventor 刘苏宣东董静
Owner CHINA PETROLEUM & CHEM CORP