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Catalyst for preparing ethanol through acetic acid hydrogenation and preparation method thereof

A catalyst and hydrogen preparation technology, applied in the chemical field, can solve the problems of high price, difficult to improve conversion rate and selectivity at the same time, limited prospects, etc., and achieve the effects of low production cost, excellent activity and selectivity, and good repeatability

Pending Publication Date: 2022-03-11
XIAMEN UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The results of existing literature show that the current main catalysts are noble metals such as Pt and Pd series, but it is difficult to improve the conversion rate and selectivity at the same time in terms of catalytic performance, and Pt and Pd are very expensive as noble metals, which will limit their industrial application. prospect

Method used

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  • Catalyst for preparing ethanol through acetic acid hydrogenation and preparation method thereof
  • Catalyst for preparing ethanol through acetic acid hydrogenation and preparation method thereof
  • Catalyst for preparing ethanol through acetic acid hydrogenation and preparation method thereof

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0029] Weigh 1.06g Cu(NO 3 ) 2 ·3H 2 O and 0.73g In(NO 3 ) 3 ·5H 2 Add O into a beaker, measure 130ml of pure water, put it into a water bath, stir at 60°C until completely dissolved, and obtain a mixed solution containing Cu and In. Take 5.0g gas phase SiO 2 Add it into the mixed solution, keep the temperature at 60°C, and keep stirring for 30 minutes to obtain a mixed solution. Dissolve 5.3g of anhydrous sodium carbonate in 500ml of water, stir to dissolve, transfer to a titration funnel, add dropwise to the above mixed solution, keep constant temperature and keep stirring during the process. Titrate until the pH value is 7.5, and the titration ends. After that, the stirring was continued for 2 h, and a solid was obtained after suction filtration, which was transferred to an oven at 120° C. for drying for 10 h to obtain solid A. Solid A was calcined at 450°C for 4 hours to obtain solid B. The solid B was pressed into tablets, and 30 to 60 mesh particles were screene...

Embodiment 2

[0033] Weigh 5.32g Cu(NO 3 ) 2 ·3H 2 O and 1.44g In(NO 3 ) 3 ·5H 2 Add O into a beaker, measure 130ml of pure water, put it into a water bath, stir at 60°C until completely dissolved, and obtain a mixed solution containing Cu and In. Take 5.0g gas phase SiO 2 Add it into the mixed solution, keep the temperature at 60°C, and keep stirring for 30 minutes to obtain a mixed solution. Dissolve 5.3g of anhydrous sodium carbonate in 500ml of water, stir to dissolve, transfer to a titration funnel, add dropwise to the above mixed solution, keep constant temperature and keep stirring during the process. Titrate until the pH value is 7.5, and the titration ends. After that, the stirring was continued for 2 h, and a solid was obtained after suction filtration, which was transferred to an oven at 120° C. for drying for 10 h to obtain solid A. Solid A was calcined at 450°C for 4 hours to obtain solid B. The solid B was pressed into tablets, and 30 to 60 mesh particles were screene...

Embodiment 3

[0036] Weigh 2.07g Cu(NO 3 ) 2 ·3H 2 O and 1.44g In(NO 3 ) 3 ·5H 2Add O into a beaker, measure 130ml of pure water, put it into a water bath, stir at 60°C until completely dissolved, and obtain a mixed solution containing Cu and In. Take 5.0g gas phase SiO 2 Add it into the mixed solution, keep the temperature at 60°C, and keep stirring for 30 minutes to obtain a mixed solution. Dissolve 5.3g of anhydrous sodium carbonate in 500ml of water, stir to dissolve, transfer to a titration funnel, add dropwise to the above mixed solution, keep constant temperature and keep stirring during the process. Titrate until the pH value is 7.5, and the titration ends. After that, the stirring was continued for 2 h, and a solid was obtained after suction filtration, which was transferred to an oven at 120° C. for drying for 10 h to obtain solid A. Solid A was calcined at 450°C for 4 hours to obtain solid B. The solid B was pressed into tablets, and 30 to 60 mesh particles were screened...

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Abstract

The invention relates to a catalyst for preparing ethanol through acetic acid hydrogenation and a preparation method of the catalyst. The catalyst comprises metal copper, a metal additive and a carrier, the metal additive is selected from at least one of indium, zinc, silver, gallium and cobalt, and the carrier is selected from at least one of silicon dioxide, carbon nanotubes, silicon carbide and activated carbon; based on the total mass of the catalyst, the mass fraction of the metal copper is 5-20%, the mass fraction of the metal additive is 1-9%, and the balance is the carrier. The catalyst is suitable for acetic acid hydrogenation reaction, glacial acetic acid and hydrogen are used as reaction raw materials, the acetic acid conversion rate is close to 100%, and the ethanol selectivity is higher than 90%. The catalyst is simple in preparation method, low in price and excellent in performance, and has a very wide industrial application prospect.

Description

technical field [0001] The invention relates to the field of chemical industry, in particular to a catalyst for hydrogenating acetic acid to prepare ethanol and a preparation method thereof. Background technique [0002] Ethanol is an important basic chemical raw material, which can be used as a fuel additive, a hydrogen carrier, and can also be used to synthesize various chemicals such as ethylene, vinyl acetate, and ethyl acetate. Acetic acid can be produced in large quantities by methanol from coal and homogeneous carbonylation of methanol. The hydrogenation of acetic acid to ethanol is considered to be an important route. At present, there are two main ways to produce ethanol by hydrogenation of acetic acid: one is to directly hydrogenate acetic acid to produce ethanol in one step; the other is to esterify acetic acid into acetate first, and then obtain ethanol through hydrogenation; The operation of the method is cumbersome, and the equipment investment is much higher...

Claims

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Application Information

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IPC IPC(8): B01J23/825B01J23/89B01J23/80B01J23/75B01J27/224C07C29/149C07C31/08
CPCB01J23/825B01J23/8926B01J23/80B01J23/75B01J27/224C07C29/149C07C31/08
Inventor 康金灿蒋德虎何顺张庆红王野
Owner XIAMEN UNIV