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A kind of highly dispersed catalytic system and its preparation method and application

A catalytic system, high dispersion technology, applied in chemical instruments and methods, hydrogenation to hydrocarbons, bulk chemical production, etc., can solve the problems of easy blockage of gas distribution pores, uneven dispersion, low hydrogenation activity, etc., to avoid acetylene The effect of deep hydrogenation, less dosage, and improved ethylene yield

Active Publication Date: 2018-01-30
BEIJING HUAFU ENG
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, those skilled in the art know that the slurry bed reactor is a gas-liquid-solid three-phase reaction, which requires uniform mixing of gas, liquid and solid, but since the fixed bed catalyst must be loaded on the carrier, its particle size is limited, and the larger particle catalyst The dispersion in the slurry is uneven; and the large particle solids are easy to block the gas distribution holes in the slurry bed; in addition, there are defects such as low hydrogenation activity, large addition, complicated preparation, and equipment wear.

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  • A kind of highly dispersed catalytic system and its preparation method and application

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Experimental program
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Embodiment 1

[0031] Specific steps are as follows:

[0032] 1) Mole ratio n (Pd) :n (Ag) =1:2.5 Get catalyst precursor palladium chloride 0.336g, cocatalyst silver nitrate to be dissolved in 2g water, obtain aqueous solution;

[0033] 2) Dissolve the surfactant fatty alcohol polyoxyethylene ether in the organic solution N-methyl-2-pyrrolidone, mix uniformly to prepare 400 g of the dispersed phase, and the concentration of the surfactant is 500 μg·g -1 ;

[0034] Raise the temperature of the dispersed phase to 80°C, and slowly add the aqueous solution into the dispersed phase under vigorous stirring;

[0035] 3) Continue to slowly raise the temperature of the mixed solution to 120°C, pass nitrogen gas for 60 minutes, and remove the water in the mixed solution by air stripping;

[0036] 4) Continue to raise the temperature to 160°C, pass in hydrogen, and the space velocity is 1s -1 , and reduced for 5 hours to obtain the catalytic system 1, the average particle size of the particles in ...

Embodiment 2

[0038] Specific steps are as follows:

[0039] 1) Take a certain amount of co-solvent nitric acid and disperse in water to obtain a total of 6g, by molar ratio n (Pd) :n (Ag) =1:1 get catalyst precursor palladium nitrate 24.3g, promoter silver nitrate and dissolve in water, prepare aqueous solution;

[0040] 2) Dissolve surfactant cetylbenzenesulfonate, ionic liquid [BMIM][BF4] 3g in organic solution dimethylformamide, mix evenly and be made into dispersed phase 100g; Wherein, surfactant concentration is 300μg·g -1 ;

[0041] Raise the temperature of the dispersed phase to 80°C, atomize and disperse the aqueous solution into the dispersed phase;

[0042] 3) Continue to slowly raise the temperature of the mixed solution to 180°C, pass nitrogen gas for 10 minutes, and remove the water in the mixed solution by air stripping;

[0043] 4) Continue to raise the temperature to 200°C, inject hydrogen with a space velocity of 0.1s -1 , and reduced for 1 h to obtain the catalytic ...

Embodiment 3

[0045] Proceed as follows:

[0046] 1) Use acetic acid as a co-solvent, configure an acetic acid solution with pH=3, by molar ratio n (Pd) :n (Ag) =1:3 get catalyst precursor palladium acetate 3.36g, cocatalyst silver nitrate and dissolve in the acetic acid aqueous solution of 3g, be mixed with aqueous solution;

[0047] 2) Surfactant alkyl sulfonate, ionic liquid [BMIM] [BF4 ]3g was dissolved in the organic solution dimethylformamide, uniformly mixed to form 900g of the dispersed phase, wherein the surfactant concentration was 300μg·g -1 ;

[0048] Raise the temperature of the dispersed phase to 80°C, slowly add the aqueous solution into the dispersed phase under ultrasonic vibration and stirring;

[0049] 3) Continue to slowly raise the temperature of the mixed solution to 150° C., pass nitrogen gas for 30 minutes, and remove moisture by air stripping;

[0050] 4) Continue to raise the temperature to 180°C, inject hydrogen with a space velocity of 0.5s -1 , reduced for ...

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Abstract

The invention relates to a highly dispersed catalytic system and a preparation method therefor and application thereof. The catalytic system is prepared by the steps: dissolving catalyst precursor water-soluble palladium salt and a co-catalyst solution in water to obtain an aqueous solution; and then dispersing the aqueous solution in a dispersed phase, and carrying out gas stripping and temperature-rising reduction, wherein, the quality content of metal palladium in the obtained catalytic system is 0.1-1%; and the particle diameter of the catalytic system is between 1 nm-100 nm. The obtained catalytic system does not have a carrier. When the system is used in an acetylene to ethylene process, the system is small in use level, low in cost, high in effective coefficient and high in space time yield, so that acetylene deep hydrogenation is avoided, and the acetylene conversion rate and the ethylene yield are improved; and meanwhile, the defects that large solid particles are likely to promote bubble coalescence to block a gas distributor and cause equipment wear and the like are overcome, and vapor, liquid and solid phases of a slurry reactor are uniformly distributed preferably.

Description

technical field [0001] The invention relates to a highly dispersed catalytic system and its preparation method and application, and belongs to the technical field of petrochemical product synthesis and novel catalytic materials. Background technique [0002] Ethylene is the most important basic raw material in petrochemical industry, known as "the mother of petrochemical industry". At present, it is mainly produced by cracking petroleum or low-carbon alkanes. However, the ethylene from the naphtha cracking furnace contains a small amount of acetylene, which has a toxic effect on the subsequent ethylene polymerization reaction, so it is necessary to reduce the acetylene content to below 10ppm. [0003] Current research shows that the use of acetylene hydrogenation to ethylene slurry bed process to remove acetylene in ethylene is an important development direction. The prior art discloses a method for preparing ethylene by liquid-phase selective hydrogenation of acetylene in...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/50C07C11/04C07C5/09
CPCY02P20/52Y02P20/54
Inventor 余海鹏史雪君吴道洪
Owner BEIJING HUAFU ENG