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

A catalyst and a technology for producing ethanol, which are applied in chemical instruments and methods, preparation of hydroxyl compounds, preparation of organic compounds, etc., can solve the problem of decreased catalyst stability, low acetic acid conversion rate, catalyst acetic acid conversion rate and ethanol selectivity. 95% and other problems, to achieve the effect of low production cost and simple production and preparation method

Pending Publication Date: 2021-10-26
CHNA ENERGY INVESTMENT CORP LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The test shows that the catalyst has shown better ethanol selectivity in the reaction process of hydrogenation of acetic acid to ethanol, but the conversion rate of acetic acid is lower than 85%.
And as the reaction proceeds, the stability of the catalyst decreases
[0008] CN102600871A discloses that active components are supported on silicon oxide, activated carbon, aluminum oxide, titanium dioxide and other carriers by impregnation method. The catalyst prepared by this method shows better activity, but the acetic acid conversion rate and The ethanol selectivity has not all reached more than 95%, and the stability of the catalyst is yet to be investigated

Method used

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

Examples

Experimental program
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Effect test

Embodiment 1

[0059] Step (1): Add 8.0g of ammonium molybdate and 6.2g of ammonium dihydrogen phosphate into 200mL of deionized water, heat and dissolve at 90°C under constant stirring, and obtain a clear and transparent Mo-P mixed solution;

[0060] Step (2): Weigh 70g Al 2 o 3 and 10g of MgO, mixed in a ball mill, ground for 2 hours, and then fired at 1000°C for 8 hours to obtain magnesium aluminum spinel.

[0061] Step (3): 100g of high-purity SiO after roasting at 500°C 2 Mix the powder, 6g of safflower powder and 10g of magnesia-aluminum spinel in step (2) evenly, pour it into the kneader, slowly add the mixed liquid in step (1) while kneading, knead and extrude into 3mm*5mm After the rod-shaped shape, put it into a 120°C drying oven for 6 hours, and finally bake it in a 600°C muffle furnace for 4 hours to obtain the acetic acid hydrogenation catalyst carrier, and its specific surface area measured by BET is 181m 2 / g.

[0062] Step (4): Add the catalyst carrier obtained in step (3...

Embodiment 2

[0065] Step (1): Add 8.0g of ammonium molybdate and 6.2g of ammonium dihydrogen phosphate into 200mL of deionized water, heat and dissolve at 90°C under constant stirring, and obtain a clear and transparent Mo-P mixed solution;

[0066] Step (2): take by weighing 12.82g Mg(NO 3 ) 2 ·6H 2 O, 37.51g Al(NO 3 ) 3 9H 2 O was dissolved in 100mL deionized water and stirred to form a solution. Under vigorous stirring, ammonia water with a concentration of 25% by mass was slowly dropped in, and after white flocculent precipitation appeared, the pH value of the slurry was controlled at about 10. The precipitate was filtered and washed twice with deionized water, then dried in a drying oven at 120°C for 12 hours, and finally calcined in a muffle furnace at 700°C for 5 hours to obtain magnesium aluminum spinel.

[0067] Step (3): 10 g of magnesium-aluminum spinel obtained in step (2) is directly mixed with 100 g of high-purity alumina powder and 6 g of turnip powder, poured into a k...

Embodiment 3

[0071] Step (1): Add 8.0g of ammonium molybdate and 6.2g of ammonium dihydrogen phosphate into 200mL of deionized water, heat and dissolve at 90°C under constant stirring, and obtain a clear and transparent Mo-P mixed solution;

[0072] Step (2): 33.76g Al(NO 3 ) 3 9H 2 O with 12.82g Mg(NO 3 )2·6H 2 O was dissolved in a mixed solution of 80ml of deionized water and 40ml of ethanol, and was stirred to form a solution; 25.2g of urea and 2.02g of sodium lauryl sulfate were added to the above solution, and stirred for 30min; the resulting solution was transferred to a volume of 200ml In a polytetrafluoroethylene-lined stainless steel autoclave, the reaction was carried out at a constant temperature of 180 ° C for 8 h, and then naturally cooled to room temperature. After the product was filtered, it was washed three times with deionized water and absolute ethanol, respectively. Then dry at 120°C, and then bake at 700°C for 4 hours to obtain magnesium-aluminum spinel;

[0073]...

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Abstract

The invention provides a catalyst for preparing ethanol through acetic acid hydrogenation. The catalyst comprises, by weight, 30-60% of transition metal; 5-40% of P; 1-20% of spinel; and 14%-58% of a carrier. The invention provides a preparation method of the catalyst. The method comprises the following steps: (1) mixingthe carrier and spinel, molding, drying and roasting to obtain a molded body; and (2) dipping the molded body by using a mixed solution containing transition metal and phosphorus salt, and then drying and roasting. The invention provides a method for preparing ethanol through acetic acid hydrogenation. The catalyst is mild in reaction condition, high in acetic acid conversion rate, high in ethanol selectivity and good in catalyst stability when applied to acetic acid hydrogenation synthesis of ethanol.

Description

technical field [0001] The invention relates to a catalyst for hydrogenation of acetic acid to produce ethanol, a preparation method thereof and a method for hydrogenation of acetic acid to produce ethanol. Background technique [0002] Ethanol is an important chemical product and chemical intermediate. There is a great demand for ethanol in the chemical industry. Ethanol has obvious advantages as a petroleum additive and is currently the most important fuel additive in the world. my country has promoted fuel ethanol pilot projects all over the country. The production method of fuel ethanol in my country is mainly the bio-fermentation method of corn and wheat, which leads to two disadvantages of high cost and threat to national food security in the industrial development of fuel ethanol: first, the cost of producing ethanol by grain method is higher than that of fuel ethanol The market price is at a loss. Second, unlike the United States and Brazil, which are large agricultu...

Claims

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Application Information

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IPC IPC(8): B01J27/19B01J27/195C07C29/149C07C31/08
CPCB01J27/19B01J27/195C07C29/149C07C31/08
Inventor 龙俊英田树勋张雪冰
Owner CHNA ENERGY INVESTMENT CORP LTD