Catalyst for synthesizing dimethyl ether one-step with synthesis gas as well as its preparing method

A synthesis gas and catalyst technology, which is applied in ether preparation, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problem that methanol synthesis active components and molecular sieves cannot achieve highly uniform mixing, catalysts are easy to agglomerate, and stay in the mechanical Mixing and other issues to achieve the effect of high activity and selectivity, good reproducibility, and controllable pore structure

Inactive Publication Date: 2008-04-09
TAIYUAN UNIV OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the preparation of this type of catalyst is still in the stage of mechanical mixing, and the methanol synthesis active components and molecular sieves cannot achieve highly uniform mixing
In the slurry bed reactor, the two components of the catalyst prepared by this method will be further separated during the reaction process, the synergistic effect between the components will become poor, and the catalyst will easily agglomerate, agglomerate, and deactivate

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment approach 1

[0017] Dissolve ethyl orthosilicate in ethanol, stir at room temperature at 700r / min; weigh a certain amount of aluminum nitrate, copper nitrate, zinc nitrate to make a mixed solution, and slowly drop it into the solution of ethyl orthosilicate In the ethanol solution; after it is mixed evenly, slowly drop in the aqueous solution of hexamethylenediamine to make it completely precipitate; continue to stir, and add dilute nitric acid to adjust the pH value of the solution until the solution is clear, and a uniform and transparent sol is obtained at this time. When placed at 40°C for 20 hours, the sol lost its fluidity and became a gel. After aging at room temperature for 10 days, mix it with liquid paraffin evenly, add span80 as an antifoaming agent, program the temperature to 300°C under nitrogen atmosphere, and keep stirring at 500r / min for 9 hours to prepare a slurry catalyst. Depending on the ratio of silicon to aluminum, the catalyst can be made into cat50, cat25, cat12, ca...

Embodiment approach 2

[0019] Dissolve ethyl orthosilicate in ethanol, stir at room temperature at 700r / min; weigh a certain amount of aluminum nitrate to make an aqueous solution and slowly drop it into the ethanol solution of ethyl orthosilicate; wait until it is evenly mixed Finally, slowly drop in the aqueous solution of hexamethylenediamine to make it completely precipitate; stir at 90°C, and add dilute nitric acid to adjust the pH value of the solution until the solution is clear, and a uniform and transparent sol is obtained at this time. Slowly drop a certain amount of mixed solution of copper nitrate and zinc nitrate into the sol and continue stirring until it becomes a uniform and transparent sol again. The solvent was distilled off at 200°C to form a gel. The follow-up method is the same as Embodiment 1, and a cat2-2 type catalyst is produced.

Embodiment approach 3

[0021] Dissolve aluminum nitrate in water and stir at room temperature at 700r / min; weigh a certain amount of ethyl orthosilicate to make ethanol solution and slowly drop it into the aqueous solution of aluminum nitrate; after it is mixed evenly, slowly drop Add hexamethylenediamine aqueous solution to make it completely precipitate; stir at 60°C, and add dilute nitric acid to adjust the pH value of the solution until the solution is clear. At this point a homogeneous, transparent sol was obtained. Slowly drop a certain amount of mixed solution of copper nitrate, zinc nitrate and additive magnesium nitrate into the sol and continue stirring until it becomes a uniform and transparent sol again. After aging at 200°C for 10 days, mix it with liquid paraffin evenly, add Tween as a defoamer, program the temperature to 300°C under air atmosphere, and keep stirring at 500r / min for 9h to prepare a slurry catalyst. According to different additives, the catalyst can be made into cat2-M...

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PUM

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Abstract

The invention relates to catalyst synthesizing dimethyl ether with synthetic gas in one step and the preparation method thereof, and belongs to the catalyst preparation technical field. The invention is characterized in that a methanol synthetic component and a methanol dehydration component are prepared in a one pot way under the same condition, active components of Cu and Zn are added in the liquid phase condition, and Si-Al oxide, molecular sieve, and a silica resource, an aluminum resource, and template agent required by organic-inorganic hybrids of Si or Si-Al are formed under the liquid phase completely, and thus slurried catalyst with the general formula which is CuZnMSiAl (M is auxiliary agent) is prepared. The environmental change and the phase change are not required during the preparing process, the operation is simple, the repeatability is good, the pore structure can be controlled, the activity is high, and the preparation method is especially suitable for preparing the catalyst used by a slurry bed reactor.

Description

technical field [0001] The invention discloses a catalyst for synthesizing dimethyl ether by one-step synthesis gas and a preparation method thereof, belonging to the technical field of catalyst preparation. Specifically, it relates to a method for preparing a catalyst for directly synthesizing dimethyl ether from synthesis gas in a slurry state composed of Si, Al and other components. Background technique [0002] At present, the main preparation method of a one-step dimethyl ether synthesis catalyst is to combine a methanol synthesis catalyst and a methanol dehydration catalyst. The former mostly uses copper-based catalysts, the main components are Cu and Zn, and a small amount of Al 2 o 3 As a structural aid; the latter mainly consists of acidic dehydrating components. Molecular sieves are widely used as methanol dehydration catalysts because of their rich microporous structure, large specific surface area, good adsorption performance and surface acidity. However, at ...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/80B01J23/83B01J23/889C07C43/04C07C41/01
Inventor 黄伟任杰樊金串高志华谢克昌
Owner TAIYUAN UNIV OF TECH
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