Catalyst used in process of preparing furfuryl alcohol by furfural through selective hydrogenation and preparation method of catalyst

A technology for selective hydrogenation and catalysts, applied in chemical instruments and methods, metal/metal oxide/metal hydroxide catalysts, physical/chemical process catalysts, etc. Complex, high cost of catalyst raw materials, to achieve the effect of low cost, high activity and selectivity, and long service life

Inactive Publication Date: 2013-04-03
ZHUHAI KAIMEI TECH
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

The current hydrogenation catalysts mainly include Cu-Cr, modified Cu-Cr and Raney Ni, etc. Cr-containing catalysts are not only very expensive, but also have high toxicity because the copper-chromium oxide catalyst used is discharged from the reactor with the hydrogenation product , causing serious pollution to the environment, or separation and regeneration are difficult, and it is easy to block the reactor. Although the Raney Ni catalyst has high activity, it is easy to produce by-products, and the catalyst preparation process involves alkali extraction of aluminum, which will also cause certain environmental pollution. Pollution
Some existing documents, such as the catalysts reported in patent numbers ZL 200510122916.5 and 201210090013.3, can solve some problems, but there is still a certain amount of Cr, which does not completely eliminate the impact of Cr on the environment
The document ZL200510011872.9 also reported a catalyst that does not contain Cr, but it not only has a copper oxide content higher than 45%, but also contains TiO 2 It will inevitably cause the cost of catalyst raw materials to be too high. At the same time, TiO 2 The purity has a great influence on the activity of the catalyst, for TiO 2 Refined and SiO 2 The mixing process requires high requirements, which makes the catalyst preparation process complicated

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0023] 13.3 grams of copper nitrate and 100ml of water are stirred in a round bottom flask, titrated with 10% sodium hydroxide to form mixed colloid A, and industrial silica sol (40% SiO 2 ) 39g and 78g of water to dilute to form colloid B, add the colloid B to the colloid A, heat up to 80°C for aging for 4 hours, then filter and wash, then dry at 120°C for 16 Hours, and then baked at 600°C for 4 hours to form a copper oxide-silicon oxide composite oxide, the content of the copper oxide is 20wt%, at a temperature of 160-450°C, use hydrogen or hydrogen / nitrogen mixed gas Reductively activate the composite oxide of copper oxide-silicon oxide for 3-18 hours to prepare a catalyst, and react at a temperature of 60°C, a pressure of 1.0MPa, and a 20% furfural methanol solution according to the loading amount of the catalyst of 10ml. The conversion rate of furfural was 98.0%, and the selectivity of furfuryl alcohol was 99.5%.

Embodiment 2

[0025] 18.2 grams of copper nitrate and 130ml of water are stirred in a round-bottomed flask, titrated with 15% sodium hydroxide to form mixed colloid A, and industrial silica sol (40% SiO 2 ) was diluted with 35g of water and 70g of water to form colloid B, and the colloid B was added to the colloid A, and aged at 80°C for 4 hours, then filtered and washed, and dried at 120°C for 16 hours. Calcined at 600°C for 4 hours to form a composite oxide of copper oxide-silicon oxide, the content of the copper oxide is 25wt%. Copper oxide-silicon oxide composite oxide is reductively activated for 3-18 hours to prepare the catalyst. According to the filling amount of 10ml catalyst, it is reacted under the conditions of temperature 90℃, pressure 0.05MPa, and 20% furfural methanol solution. The conversion rate of furfural is 99.5%, and the selectivity of furfuryl alcohol is 98.5%.

Embodiment 3

[0027] 42.1 grams of copper nitrate and 300ml of water are stirred in a round-bottomed flask, titrated with 20% sodium hydroxide to form mixed colloid A, and industrial silica sol (40% SiO 2 ) was diluted with 35g of water and 70g of water to form colloid B, and the colloid B was added to the colloid A, and aged at 80°C for 4 hours, then filtered and washed, and dried at 120°C for 16 hours. Baking at 600°C for 4 hours to form a composite oxide of copper oxide-silicon oxide, the content of the copper oxide is 30wt% at a temperature of 160-450°C, using hydrogen or hydrogen / nitrogen mixed gas to treat the Copper oxide-silicon oxide composite oxide is reductively activated for 3-18 hours to prepare the catalyst. According to the filling amount of 10ml catalyst, it is reacted under the conditions of temperature 120°C, pressure 0.05MPa, and 20% furfural methanol solution. The conversion rate of furfural is 99.5%, and the selectivity of furfuryl alcohol is 98.5%.

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Abstract

The invention discloses and provides a catalyst used in a process of preparing furfuryl alcohol by furfural through selective hydrogenation and a preparation method of the catalyst, wherein the catalyst has the advantages of lower cost, capability of protecting environment, low reaction temperature, long service life and high activity and selectivity. The catalyst is a copper oxide-silicon oxide compound oxide. The preparation method comprises the steps of: 1, adding water in a copper salt, stirring for dissolving, and reacting by using 10-20 weight percent of sodium hydroxide solution to form a colloid A; 2, diluting the silicon oxide colloid by using water accounting for two times of the silicon oxide colloid by weight to form a colloid B; 3, adding the colloid B into the colloid A, mixing, sequentially heating, ageing, filtering, washing, drying and roasting; and 4, carrying out hydrogenation reduction activation for 3-18h to prepare the catalyst. The catalyst does not contain a toxic material Cr, can react at a low temperature, is capable of reducing the production energy consumption, and is high in reaction activity, high in furfural transformation rate, and high in selectivity of furfuryl alcohol.

Description

technical field [0001] The invention relates to a catalyst for preparing furfuryl alcohol through selective hydrogenation of furfural and a preparation method thereof. Background technique [0002] Furfuryl alcohol, chemical name furan methanol, 2-hydroxymethyl furan, is an important organic raw material. Furfuryl alcohol is mainly used in the production of furfural resin, furan resin, modified urine aldehyde and phenolic resin, etc. It is also a good solvent for resins, varnishes, and pigments. It can also be used for molding and core making in casting production. It is used in synthetic fibers, rubber, and pesticides. Also has a wide range of uses. The resin after furfuryl alcohol polymerization has high strength, good heat resistance and water resistance, and has good resistance to acids, alkalis, salts and organic solutions. It is an excellent binder for porous materials such as wood, rubber, metal and ceramics. Furfuryl alcohol is the most important species of fur...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J23/72C07D307/44
Inventor 刘兰崔健崔晓桐
Owner ZHUHAI KAIMEI TECH
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