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Catalyst for preparing ethane and hexane through butene disproportionation

A catalyst, catalyst carrier technology, applied in physical/chemical process catalysts, metal/metal oxide/metal hydroxide catalysts, chemical instruments and methods, etc., can solve the problems of low selectivity of ethylene and hexene and high reaction temperature

Active Publication Date: 2008-08-06
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 high reaction temperature and low selectivity of ethylene and hexene in the prior art, and a new catalyst for producing ethylene and hexene by disproportionation of butene is provided

Method used

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  • Catalyst for preparing ethane and hexane through butene disproportionation
  • Catalyst for preparing ethane and hexane through butene disproportionation
  • Catalyst for preparing ethane and hexane through butene disproportionation

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0022] Weigh 50 grams of γ-Al after roasting and drying 2 o 3 (the specific surface area is 278 square meters per gram), put it into a dry glass beaker, accurately measure 43 milliliters of rhenium with a pipette and put it in another beaker, and then add 7 ml of deionized water, and stir well.

[0023] Quickly pour the above perrhenic acid solution into the γ-Al 2 o 3 In a beaker, stir well and let stand for 4 hours, and dry at 120°C for 10 hours. Place the above-mentioned prepared sample in a tube furnace and feed dry air, the gas flow rate is controlled at 1000 mg / min, the temperature is raised to 550°C at a rate of 10°C / min and roasted, and kept for 8 hours, the obtained rhenium content is 6%. Re 2 o 7 / Al 2 o 3 Catalyst samples.

Embodiment 2

[0025] Weigh 50 grams of γ-Al after roasting and drying 2 o 3 (the specific surface area is 278 square meters per gram), put into a dry glass beaker, and accurately measure the concentration of 50 milliliters of rhenium with a pipette and be that the perrhenic acid aqueous solution of 70 milligrams per milliliter is placed in another beaker. Quickly pour the above perrhenic acid solution into the γ-Al 2 o 3 In a beaker, stir well and let stand for 4 hours, and dry at 120°C for 10 hours.

[0026] Accurately measure 7 milliliters of rhenium perrhenic acid aqueous solution with a concentration of milligrams per milliliter with a pipette and place it in a beaker, then add deionized water to make the solution volume 50 milliliters. The second impregnation was carried out as above and dried at 120°C for 10 hours. Carry out catalyst sample roasting by the method described in embodiment 1, the content of making rhenium is 8% Re 2 o 7 / Al 2 o 3 Catalyst samples.

Embodiment 3~7

[0028] The content of making rhenium respectively by the method for embodiment 2 is 10%, 12%, 14%, 16%, 20% Re 2 o 7 / Al 2 o 3 catalyst samples.

[0029] It is 60 centimeters in length, and the inner diameter is 1.8 centimeters of reactor bottoms to add volume and be 80 cubic centimeters, particle size is 10~20 order glass ball fillers; 2 grams of Re 2 o 7 / Al 2 o 3 The catalyst is added to the reactor, and 30 cubic centimeters of glass ball fillers with a particle size of 10 to 20 meshes are added to the top of the catalyst. The temperature of the reactor was raised to 550° C. under the condition of feeding 10 liters of nitrogen per hour, and kept at this temperature for 2 hours, and then dropped to a reaction temperature of 40° C.

[0030] The reactor stops feeding nitrogen, and feeds 99.5% 1-butene raw material from the upper end of the reactor, the raw material flow rate is 10 ml / hour, and the reaction system pressure is controlled at 3MPa by the regulating valve at...

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Abstract

A catalyst for dismutating butene to prepare ethene and hexene with high selectivity and the ability to suppress the double-bond isomerizing reaction of 1-buten is composed of the carrier chosen from Al2O3, SiO2 and TiO2 and the active component chosen from Re, Mo and Co.

Description

technical field [0001] The invention relates to a catalyst for producing ethylene and hexene by disproportionation of butene. Background technique [0002] 1-Hexene is an important additive for the synthesis of linear low-density polyethylene with high added value; butene is a by-product of steam cracking of naphtha and is generally consumed as liquefied petroleum gas. Through the self-disproportionation reaction of butene and the isomerization reaction of olefins, relatively excess butene with low added value can be converted into hexene and ethylene with high added value. The reaction formula is as follows: [0003] The first step: butene isomerization reaction: [0004] <chemistry num="0001"> <chem file="200510028793_CML001.XML" / > < / chemistry> [0005] The second step: self-disproportionation reaction of 1-butene: [0006] <chemistry num="0002"> <chem file="200510028793_CML002.XML" / > < / chemistry> [0007] The third step: 3-...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/28B01J23/75B01J23/882C07C6/04C07C11/04C07C11/107
CPCY02P20/52
Inventor 徐炜谢在库王仰东刘苏徐舟波
Owner CHINA PETROLEUM & CHEM CORP