Vanadium phosphorus oxide (VPO) catalyst and application thereof in preparation of acraldehyde from glycerol in dewatering manner

A catalyst and acrolein technology, applied in the direction of physical/chemical process catalysts, carbon-based compound preparation, organic compound preparation, etc., to achieve high activity effect

Inactive Publication Date: 2014-05-21
NANJING UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

At present, the reaction of dehydration of glycerol to prepare acrolein is still in the laboratory stage, and the catalyst activity (conversion rate) and selectivity are mainly improved.

Method used

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  • Vanadium phosphorus oxide (VPO) catalyst and application thereof in preparation of acraldehyde from glycerol in dewatering manner
  • Vanadium phosphorus oxide (VPO) catalyst and application thereof in preparation of acraldehyde from glycerol in dewatering manner
  • Vanadium phosphorus oxide (VPO) catalyst and application thereof in preparation of acraldehyde from glycerol in dewatering manner

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0020] The mixed solution of 4.8g vanadium pentoxide and 72ml benzyl alcohol and isobutanol (1:1 volume ratio) was refluxed at 140°C for 6 hours, and 6.69g concentrated phosphoric acid with a concentration of 85% by mass was added, and then refluxed for 6 hours , the obtained dark blue suspension mixture was filtered, the solid was washed with acetone, and dried at 100° C. for 24 hours to obtain a catalyst precursor. The dried catalyst was pressed into tablets and crushed to obtain 60-80 mesh particles for activity testing.

[0021] Take 0.5g of the above catalyst, and carry out the continuous reaction of glycerol dehydration to produce acrylic acid in a fixed-bed reactor. The meter is passed into the catalyst bed, the reaction material is 36.5% glycerol aqueous solution, and the liquid space velocity is 4h -1 . Sampling and chromatographic analysis after 2 hours showed that the conversion rate of glycerin was 72.0%, the yield of acrolein was 23.3mol%, and the generation rat...

Embodiment 2

[0023] A mixed solution of 4.8g of vanadium pentoxide and 72ml of benzyl alcohol and isobutanol (1:1 by volume) was refluxed at 140°C for 6 hours, 2.1g of PEG6000 was added, and after one hour, 6.69g of PEG6000 was added with a mass percent concentration of 85 % concentrated phosphoric acid, and then reflux for 6 hours, filter the resulting dark blue suspension mixture, wash the solid with acetone, and dry at 100°C for 24 hours to obtain the catalyst and press it into tablets and crush it to obtain 60-80 mesh particles, which are used for active test.

[0024] Take 0.5g of the above catalyst, and carry out the continuous reaction of glycerol dehydration to produce acrylic acid in a fixed-bed reactor. The meter is passed into the catalyst bed, the reaction material is 36.5% glycerol aqueous solution, and the liquid space velocity is 4h -1 . After 2 hours, sampling and chromatographic analysis showed that the conversion rate of glycerin was 93.3%, the yield of acrolein was 18....

Embodiment 3

[0026] 4.8g of vanadium pentoxide and 72ml of benzyl alcohol were refluxed at 140°C for 6 hours, 2.1g of PEG6000 was added, and after one hour, 6.69g of concentrated phosphoric acid with a concentration of 85% by mass was added, and then refluxed for 6 hours, and the obtained dark blue suspension The turbid mixture was filtered, the solid was washed with acetone, and dried at 100° C. for 24 hours to obtain a catalyst precursor. The obtained sample was pressed into tablets and crushed to obtain 60-80 mesh particles for activity testing.

[0027] Take 0.5g of the above catalyst, and carry out the continuous reaction of glycerol dehydration to produce acrylic acid in a fixed-bed reactor. The meter is passed into the catalyst bed, the reaction material is 36.5% glycerol aqueous solution, and the liquid space velocity is 4h -1 . Sampling chromatographic analysis after 2h showed that the conversion rate of glycerin was 88.7%, the yield of acrolein was 23.3%, and the generation rate...

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Abstract

The invention discloses a vanadium phosphorus oxide (VPO) catalyst for preparation of acraldehyde from glycerol in a dewatering manner. The catalyst is prepared by the following steps: restoring pentavalent vanadium (vanadium pentoxide) through alcohols; adding a polyethylene glycol (PEG6000) surfactant to alcohol medium, and then adding a phosphoric acid; adjusting the P/V molar ratio to 1.1 to prepare a catalyst precursor; activating the catalyst precursor by different flows of 1.5vol.% butane-air atmosphere; adding PEG and/or changing the variety of reaction medium in the preparation process of the catalyst; modulating the phase morphology of the catalyst, the reduction behavior of lattice oxygen, and surface V5<+>/V4<+>, so that the reaction activity of the catalyst is significantly modulated. The catalyst for preparing acraldehyde from glycerol in the dewatering manner is high in activity, and is a high-efficiency catalyst for target reaction, the glycerol can be completely transformed, and the yield of the acraldehyde can be up to 70.1%.

Description

technical field [0001] The invention relates to a VPO catalyst and its application in glycerol dehydration to produce acrolein. Background technique [0002] Acrolein is the simplest unsaturated aldehyde and an important organic chemical intermediate. Acrolein is easily oxidized to acrylic acid with large market capacity and high added value. In industry, acrolein is mainly produced through the gas-phase oxidation of propylene. In the presence of bismuth molybdate and bismuth phosphomolybdate catalysts, the mixed gas of propylene and air (the molar ratio of propylene to oxygen is 6-8) is passed into the fixed bed or fluidized bed reactor, and the reaction temperature is 300-400°C , pressure 0.2 ~ 0.3MPa, the reaction in addition to produce acrolein, there are also a small amount of acetaldehyde, acetic acid, propionaldehyde, acetone and acrylic acid produced. The industrial production method of acrolein is mainly propylene oxidation, and propylene mainly comes from petrol...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): B01J27/198C07C47/22C07C45/52
Inventor 季伟捷冯新振赵亮苏秦姚瑶顾书圣
Owner NANJING UNIV
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