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Catalyst for preparing 1,3-butanediol by hydrogenation of 3-hydroxybutyraldehyde, preparation method and application thereof

A technology of hydroxybutyraldehyde and catalyst, which is applied in the field of 3-hydroxybutyraldehyde hydrogenation preparation 1, which can solve the problems of increasing the difficulty of product separation and refining, dehydration or even polymerization of 3-hydroxybutyraldehyde, affecting product yield and purity, etc. , to achieve high stability, long service life, and prevent agglomeration

Active Publication Date: 2022-05-24
ZHEJIANG HENGYI PETROCHEMICAL RES INST CO LTD +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, the traditional Raney nickel catalyst has low activity and requires a higher reaction temperature (above 100°C)
Although there is a patent report that metal nickel can be loaded to increase the reactivity, the alumina catalyst used is acidic, which easily causes the dehydration or even polymerization of 3-hydroxybutyraldehyde, which seriously affects the yield and purity of the product and increases the product yield. Difficulty in separating and refining

Method used

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  • Catalyst for preparing 1,3-butanediol by hydrogenation of 3-hydroxybutyraldehyde, preparation method and application thereof
  • Catalyst for preparing 1,3-butanediol by hydrogenation of 3-hydroxybutyraldehyde, preparation method and application thereof
  • Catalyst for preparing 1,3-butanediol by hydrogenation of 3-hydroxybutyraldehyde, preparation method and application thereof

Examples

Experimental program
Comparison scheme
Effect test

preparation example Construction

[0048] A Pt / CeO 2 The preparation method of catalyst comprises the following steps:

[0049] (1) Dissolve cerium nitrate hexahydrate in deionized water, add urea and stir to dissolve. The solid-liquid ratio of the cerium nitrate hexahydrate to deionized water is 8-9 g / 30mL, and the mass ratio of the cerium nitrate hexahydrate to the urea is 8-9:0.2.

[0050] (2) adding the citric acid solution (150-250 mg / L) to the solution obtained in step (1), and stirring evenly; the volume ratio of the solution obtained in step (1) to the citric acid solution is 25-35:2.

[0051] (3) Adjust pH=9.5-10.5 of the solution obtained in step (2), and stir for 20-40 min.

[0052] (4) Load the solution obtained in step (3) into a reaction device, seal and react at 150-160° C. for 20-30 hours, cool down to room temperature after the reaction, centrifuge the precipitate, wash with water until neutral, 50-70 °C drying.

[0053] (5) calcining the precipitate obtained in step (4) at 400-600 ° C for ...

Embodiment 1

[0061] 8.68g of cerium nitrate hexahydrate (Ce(NO 3 ) 3 ·6H 2 O) was dissolved in 60 mL of deionized water, and 0.2 g of urea (CO (NH) was added. 2 ) 2 ), stir and dissolve; then add 2mL citric acid solution (200mg / L), stir evenly, add ammonia water dropwise, adjust pH to 10, continue stirring for 30min; react in 155℃ oven for 24h; Centrifugal separation, washed with water to neutrality, and dried at 60 °C; the obtained precipitate was ground and then calcined in air, the heating rate was 5 °C / min, raised to 500 °C, and calcined for 3 h to obtain a cerium oxide carrier; Weigh CeO 2 1 g of carrier, 2 mL of water was added. Stir for 30 min and sonicate for 30 min. Add 0.5 ml of a chloroplatinic acid solution containing 0.1 g / mL of platinum, and stir for 1 h. Put it into an oven at 80 °C to dry; grind the dried sample, put it into a reduction furnace, and put it in a 5% H 2 5%Pt / CeO can be obtained by reducing at 250℃ for 1h in / Ar atmosphere 2 catalyst.

[0062] Dispers...

Embodiment 2

[0067] With reference to the same catalyst preparation and reaction steps in Example 1, the difference is that the volume of 0.1g / mL chloroplatinic acid solution containing platinum is added to be 0.2-0.8ml, and the reaction time is 1.5h to obtain catalysts with different platinum loadings. The conversion rate of 3-hydroxybutyraldehyde and the yield of 1,3-butanediol are shown in Table 2.

[0068] Table 2. Pt / CeO with different platinum loadings 2 The conversion of 3-hydroxybutyraldehyde and the yield of 1,3-butanediol obtained under

[0069] catalyst 2%Pt / CeO 2

[0070] The results in Table 2 show that on the ceria support, the most suitable Pt loading is 5% (weight ratio), and excess Pt may lead to the deep hydrogenation of part of the product 1,3-butanediol.

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Abstract

The invention relates to the technical field of catalytic hydrogenation, and discloses a catalyst for preparing 1,3-butanediol by hydrogenation of 3-hydroxybutyraldehyde and its preparation method and application. The Pt / CeO 2 The catalyst can be used for the hydrogenation of 3-hydroxybutyraldehyde to prepare 1,3-butanediol, which has the characteristics of high reactivity, high selectivity and good stability, and can be efficiently produced by using a reactor in a hydrogen atmosphere at a lower temperature Hydrogenation of 3-hydroxybutyraldehyde to 1,3-butanediol. The present invention adopts solvothermal method to prepare CeO 2 The carrier is prepared by impregnating and supporting Pt, and the preparation method is simple. In addition, the present invention can produce 1,3-butanediol with high conversion rate and high selectivity by optimizing the hydrogenation process.

Description

technical field [0001] The invention relates to the technical field of catalytic hydrogenation, in particular to a catalyst for preparing 1,3-butanediol by hydrogenation of 3-hydroxybutyraldehyde, a preparation method and application thereof. Background technique [0002] 1,3-Butanediol (1,3-BDO) has good hygroscopicity and water solubility, and is odorless and low in toxicity. It can be used as a moisturizing agent, an antibacterial agent, and used in the production of cosmetics and pharmaceuticals. At the same time, 1,3-butanediol can also be used to produce unsaturated polyester resins, plasticizers, moisturizing agents and softeners, etc., and has a wide range of applications in industrial production. [0003] At present, the synthesis methods of 1,3-butanediol mainly include biological method and chemical synthesis method. Although the biological method has mild production conditions, high selectivity, and low waste discharge, the yield is low and it is difficult to ac...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): B01J23/63B01J35/08C07C29/141C07C31/20
CPCB01J35/08B01J23/63C07C29/141C07C31/207Y02P20/584
Inventor 赵怀远刘皓岚姜媛媛周茹茹叶恒舒郑丽萍杜玮辰侯昭胤
Owner ZHEJIANG HENGYI PETROCHEMICAL RES INST CO LTD