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Method for propylene preparation through butane disproportionation

A technology of butene and propylene, applied in the field of butene disproportionation to propylene, can solve the problem of low catalyst activity and achieve the effects of good reaction activity and good technical effect

Active Publication Date: 2013-12-04
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 the problem of low catalyst activity in the prior art, and a new method for producing propylene by disproportionation of butene is provided

Method used

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  • Method for propylene preparation through butane disproportionation
  • Method for propylene preparation through butane disproportionation
  • Method for propylene preparation through butane disproportionation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] Weigh 500 grams of commercial MgO, add 2.5 liters of deionized water, heat and stir the resulting white turbid solution at 80°C for 5 hours, filter the water in the solution with suction, and dry the product at 120°C for 6 hours to obtain a magnesium oxide carrier.

[0024] Mix 200 grams of carrier magnesia and 1% scallop powder and put them into the blender evenly. After stirring for 12 minutes, add 19 grams of ammonium metatungstate, then add 250 grams of deionized water, knead, extrude, and dry at 550 The catalyst was prepared by calcining at ℃ for 4 hours, which was designated as SL-1.

[0025] The evaluation of the catalyst was carried out on an olefin disproportionation evaluation device, and the raw materials were 60% butene-1 and 40% 2-butene in terms of mass fraction. The reaction is at a temperature of 300°C, a pressure of 3MPa in absolute pressure, and a weight space velocity of butene of 4.8 hours -1 The evaluation was carried out under the conditions, and ...

Embodiment 2

[0028] Weigh 500 grams of commercial MgO, add 2 liters of deionized water, and heat and stir the obtained white turbid solution at 60°C for 4 hours, then let it stand for 2 hours, filter the water in the solution, and dry the product at 120°C for 4 hours to obtain the magnesium oxide carrier .

[0029] Mix 200 grams of carrier magnesia and 1% scallop powder and put them into the blender evenly. After stirring for 30 minutes, add 24 grams of ammonium metatungstate, then add 150 grams of deionized water, knead, extrude, and dry at 550 The catalyst was prepared by calcining at ℃ for 4 hours, which was designated as SL-2.

[0030] The evaluation of the catalyst is carried out on the olefin disproportionation evaluation device, the reaction is at a temperature of 350 ° C, a pressure of 2.5 MPa in absolute pressure, and a weight space velocity of butene of 6 hours -1 The evaluation was carried out under the conditions, and the evaluation results are shown in Table 1.

[0031]

Embodiment 3

[0033] Weigh 500 grams of commercial MgO, add 1.5 liters of deionized water, and heat and stir the obtained white turbid solution at 100°C for 2 hours, then let it stand for 2 hours, filter the water in the solution, and dry the product at 100°C for 8 hours to obtain a magnesium oxide carrier .

[0034] Mix 200 grams of carrier magnesia and 1% scallop powder and put them into the blender evenly. After stirring for 20 minutes, add 48 grams of ammonium metatungstate, then add 180 grams of deionized water, knead, extrude, and dry at 550 The catalyst was prepared by calcining at ℃ for 4 hours, which was designated as SL-3.

[0035] The evaluation of the catalyst was carried out on the olefin disproportionation evaluation device. The reaction was carried out at a temperature of 250°C, a pressure of 1 MPa in absolute pressure, and a weight space velocity of butene of 2 hours. -1 The evaluation was carried out under the conditions, and the evaluation results are shown in Table 1.

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Abstract

The present invention relates to a method for propylene preparation through butane disproportionation, wherein the problem of low catalyst activity in the prior art is mainly solved with the present invention. The technical scheme comprises that: 1-butene and 2-butene are adopted as raw materials, and the raw materials and a catalyst are subjected to a contact reaction in a fixed bed reactor at a reaction temperature of 200-450 DEG C under reaction pressure of 0-5 MPa (calculated as absolute pressure) at a butane weight space velocity of 1-10 h<-1> to produce a propylene-containing effluent, wherein the catalyst comprises the following components, by weight, a) 5-50 parts of tungsten oxide, and b) 50-95 parts of a magnesium oxide carrier. With the technical scheme, the problem in the prior art is well solved, and the method can be used for industrial production of propylene preparation through butane disproportionation.

Description

technical field [0001] The invention relates to a method for producing propylene by disproportionation of butene. Background technique [0002] Propylene is one of the most important basic organic raw materials second only to ethylene, and its largest use is to produce polypropylene (accounting for about half of its total), followed by the production of acrylonitrile, propylene oxide, isopropanol, and cumene , carbonyl alcohols, acrylic acid, propylene oligomers. [0003] 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 compre...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C11/06C07C6/04B01J23/30
CPCY02P20/52
Inventor 王仰东宣东刘苏
Owner CHINA PETROLEUM & CHEM CORP