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Process for preparing bifunctional catalyst for preparing dimethyl ether directly with synthesis gas

A dual-function catalyst and synthesis gas technology, applied in the direction of molecular sieve catalysts, chemical instruments and methods, physical/chemical process catalysts, etc., can solve the problems of cumbersome preparation process, long time-consuming, high temperature, etc., achieve simple preparation process and overcome cumbersome process , the effect of reducing adverse effects

Inactive Publication Date: 2008-12-03
SHANGHAI INST OF TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0008] The technical problem to be solved by the present invention is to overcome the cumbersome and time-consuming preparation process of the dimethyl ether bifunctional catalyst in the prior art, and the high temperature and low carbon monoxide conversion rate when the catalyst is used in the synthesis gas one-step method to prepare dimethyl ether. High, low selectivity of dimethyl ether, etc., provide a catalyst preparation method with simple preparation process, and the catalyst prepared by this method has the advantages of low reaction temperature, high conversion rate of carbon monoxide and good selectivity of dimethyl ether

Method used

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  • Process for preparing bifunctional catalyst for preparing dimethyl ether directly with synthesis gas

Examples

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Embodiment 1

[0035] 43.5 grams of copper nitrate, 26.8 grams of zinc nitrate and 11.2 grams of aluminum nitrate were dissolved in absolute ethanol to make a mixed solution, and 11 grams of HZSM-5 (Si / Al=60) molecular sieves as methanol dehydration components were added to the above mixed solution. solution, and then stirred thoroughly to obtain a suspension. Add an ethanol solution containing 45 grams of oxalic acid to the above suspension under stirring to obtain a precipitate. The obtained sediment is aged at room temperature for half an hour, then filtered, dried, and then calcined at 350° C. for 6 hours to obtain a catalyst powder. Finally, through tableting, crushing and sieving 20-40 mesh particles to obtain bifunctional catalyst A, wherein the weight percentage of each component is CuO 40%, ZnO 20%, Al 2 o 3 7%, H-ZSM-5 33%.

Embodiment 2

[0037] Dissolve 43.5 grams of copper nitrate, 26.8 grams of zinc nitrate and 11.2 grams of aluminum nitrate in absolute ethanol to make mixed solution a, dissolve 45 grams of oxalic acid in absolute ethanol to make solution b, and use 11 grams as methanol dehydration component The HZSM-5 (Si / Al=60) molecular sieve was added into absolute ethanol to prepare suspension c. Add solutions a and b simultaneously to the above suspension c under stirring to obtain a precipitate. The obtained sediment is aged at room temperature for half an hour, then filtered, dried, and then calcined at 350° C. for 6 hours to obtain a catalyst powder. Finally, bifunctional catalyst B was obtained by tableting, pulverizing and sieving 20-40 mesh particles, wherein the weight percentage of each component was the same as that of Example 1.

Embodiment 5

[0045] Catalysts A, B, C, D and E prepared in Examples 1, 2 and Comparative Examples 1-3 were used for gas phase reaction in a continuous flow fixed bed pressurized reaction evaluation device, and the loading amount of the catalyst was 1 g. After the catalyst is filled, the reducing gas (5% H 2 / 95%N 2 , the flow rate is 25ml / min), and the temperature is raised to 240°C. After 6 hours of reduction, the temperature of the catalyst bed is reduced to 200°C under the condition of continuing to pass the reducing gas, and then the raw material gas is switched and the temperature is gradually raised to the desired reaction temperature. temperature to react. The composition (volume fraction) of raw gas is CO: 31.1%, CO 2 : 5.7%, the rest is H 2 . The reaction conditions are pressure: 4MPa, space velocity: 1500ml / g cat h -1 . After 3 hours of reaction, the system reached equilibrium, and then samples were taken for analysis. Use HP 4890D gas chromatograph on-line, use thermal c...

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Abstract

The invention discloses two methods for directly preparing a bifunctional catalyst of dimethyl ether by synthesis gas. The core principle is to add an active component for methanol synthesis to a methanol dehydration component in an oxalate precipitation mode, for example, the following steps are adopted: a. the active component which can be used as a methanol synthesis catalyst is dissolved into alcohol in a soluble salt mode to prepare a mixed solution A; b. an active component which can be used as a methanol dehydration catalyst is added into the mixed solution A to be stirred to prepare suspension B; and c. an alcoholic solution of oxalic acid is added into the suspension B during the stirring, and a generated oxalate coprecipitate is aged, filtered, dried and finally roasted at a temperature of between 250 and 550 DEG C to prepare the bifunctional catalyst. The methods have simple preparation process, and the prepared bifunctional catalyst has low reaction temperature, high transformation rate of carbon monoxide, and good selectivity of the dimethyl ether.

Description

technical field [0001] The present invention relates to a catalyst for the preparation of dimethyl ether, more specifically to the preparation of a dual-functional catalyst used in the direct preparation of dimethyl ether by a one-step method of synthesis gas, which is composed of a methanol synthesis catalyst and a methanol dehydration catalyst method. Background technique [0002] Dimethyl ether is an important raw material for the production of various chemical products. In the 1980s, many countries in the world developed dimethyl ether as a safe atomization propellant. Freon was banned in the early 1990s, and dimethyl ether was used as an ideal substitute. In recent years, it has been found that it also has extremely good combustion performance and can achieve clean combustion. It is known as the "clean fuel" of the 21st century at home and abroad, so DME has attracted increasing attention internationally. DME was first produced by distillation of by-products in high-p...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J29/46C07C41/01C07C43/04
Inventor 毛东森卢冠忠
Owner SHANGHAI INST OF TECH
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