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Method for selectively preparing acraldehyde and hydroxy-acetone

A technology of hydroxyacetone and acrolein, which is applied to the new preparation field of supported catalysts, can solve the problems of insufficient selectivity and stability, worrying about catalyst stability, and easy coking of catalysts, so as to reduce the cost of separation and treatment, and the preparation is simple and easy to operate. , the preparation process is simple and easy to operate

Inactive Publication Date: 2013-08-14
常州市赫利来塑料有限公司
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] For the glycerol dehydration reaction, considering the recovery of the catalyst and the ease of separation of the product, heterogeneous catalysis is often used, and in order to avoid the loss of the catalyst, the gas phase dehydration is the main method, but the problem is that the catalyst is unstable at high temperature, mainly in the catalyst. It is easy to coke and deactivate. At the same time, the gas phase reaction of glycerol is carried out at high temperature, which is unfavorable from the perspective of energy consumption, and its stability is worrying for catalysts that are not resistant to temperature, such as heteropolyacids.
From the various catalysts currently developed, regardless of the form (liquid phase, gas phase, and supercritical) of glycerol catalytic dehydration, or different reactors, although catalytic species with higher activity have been found, there is more or less selectivity. And the lack of stability, especially after repeated use, it is prone to coking and serious inactivation

Method used

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  • Method for selectively preparing acraldehyde and hydroxy-acetone
  • Method for selectively preparing acraldehyde and hydroxy-acetone
  • Method for selectively preparing acraldehyde and hydroxy-acetone

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1)

[0032] Weigh 2.3g of ZSM-5 molecular sieve into the flask, then add 0.72g of copper sulfate pentahydrate and 0.85g of sodium dihydrogen hypophosphite (slightly excessive), and finally add 20mL of water, and let stand at room temperature for 1 hour . Then heated in a constant temperature water bath at 90°C with vigorous stirring until the reaction was complete. The precipitate was filtered, washed, dried and calcined at 300°C for 3h under the protection of nitrogen. Catalyst samples were prepared after cooling.

[0033] Table 1

[0034]

[0035] Weigh 0.2g of Cu / HZSM-5 molecular sieve catalysts with different loads into a 75ml reaction kettle, add 5g of glycerin, place in an extremely hot constant temperature magnetic stirrer with silicone oil, adjust the temperature to 200°C, and keep stirring at constant temperature for 2h. After the reaction is over, the product is poured into a centrifuge test tube, centrifuged and stored in an airtight manner, and analyzed by gas chr...

Embodiment 2)

[0037] Catalyst preparation is the same as the catalyst preparation part in Example 1.

[0038] Weigh 0.2g of Cu / HZSM-5 molecular sieve catalyst with 8wt% loading at different calcination temperatures in a 75ml reaction kettle, add 5g of glycerin, place it in an extremely hot constant temperature magnetic stirrer with silicone oil, adjust the temperature to 200°C, Keep stirring at constant temperature for 2h. After the reaction is over, the product is poured into a centrifuge test tube, centrifuged and stored in an airtight manner, and analyzed by gas chromatography. The results are shown in Table 2.

[0039] Table 2

[0040]

Embodiment 3)

[0042] Catalyst preparation is the same as the catalyst preparation part in Example 1.

[0043] Weigh 0.2g of 8wt% loaded Cu / HZSM-5 molecular sieve catalyst roasted at 300°C in a 75ml reaction kettle, add 5g of glycerin, place in an extremely hot constant temperature magnetic stirrer with silicone oil, and adjust to the desired Temperature, keep stirring at constant temperature for 2h. After the reaction is over, the product is poured into a centrifuge test tube, centrifuged and stored in an airtight manner, and analyzed by gas chromatography. The results are shown in Table 3.

[0044] table 3

[0045]

[0046]

[0047] nd- indicates that the component was not detected.

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Abstract

The invention discloses a catalyst for selectively preparing acraldehyde and hydroxy-acetone from biological glycerol in a controllable manner and a preparation method of the catalyst. The catalyst is prepared by adopting a novel impregnation in-situ reduction method; the Cu / HZSM-5 catalyst, which is prepared from pure glycerol by using the method, has a glycerol catalytic conversion rate of 92.1% in a reaction kettle under gentle condition and has controllable selectivity of 87.3wt% and 12.4wt% to acraldehyde and hydroxy-acetone, respectively; and 98.2wt% conversion rate for glycerol and 86.2wt% selectivity for hydroxy-acetone can be obtained by similar glycerol catalytic dehydration reaction in a reaction distillation device. The dispersed and stable catalyst, which is obtained by adopting a catalyst preparation method, is simple and easy to operate and favorable for large-scale production. Moreover, the catalytic glycerol is gentle in solvent-free dehydration reaction, high in catalytic activity, strong in controllable selectivity, and therefore, the method is a green process with advantages of environment friendliness and low cost.

Description

technical field [0001] The invention belongs to the technical field of biomass catalysis in fine chemical industry, and specifically relates to a method for selectively preparing acrolein and hydroxyacetone from biomass glycerol catalytic dehydration and a new preparation method for a supported catalyst used in the method. Background technique [0002] As the world pays attention to the environment and sustainable development, the cheap biomass resource glycerol has a large surplus with the rapid development of biodiesel, which is basically measured in millions of tons and is growing at a rate of nearly 50% every year. Glycerol is a versatile molecular cut-off that can be converted into a variety of important products or intermediates to replace non-renewable and increasingly depleted petrochemical raw materials. [0003] Acrolein and hydroxyacetone are two important chemical raw materials. Acrolein is mainly used in the production of various resins, pesticide imidacloprid,...

Claims

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Application Information

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IPC IPC(8): C07C45/52B01J37/02C07C49/17B01J37/16C07C47/22
Inventor 乐传俊顾黎萍苏扬曹桂萍
Owner 常州市赫利来塑料有限公司
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